EP3103834B1 - Ester composition and method for its manufacturing - Google Patents
Ester composition and method for its manufacturing Download PDFInfo
- Publication number
- EP3103834B1 EP3103834B1 EP15746898.4A EP15746898A EP3103834B1 EP 3103834 B1 EP3103834 B1 EP 3103834B1 EP 15746898 A EP15746898 A EP 15746898A EP 3103834 B1 EP3103834 B1 EP 3103834B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- formula
- ester
- based composition
- weight
- compound
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 150000002148 esters Chemical class 0.000 title claims description 130
- 239000000203 mixture Substances 0.000 title claims description 130
- 238000000034 method Methods 0.000 title claims description 36
- 238000004519 manufacturing process Methods 0.000 title description 9
- 150000001875 compounds Chemical class 0.000 claims description 83
- 239000004014 plasticizer Substances 0.000 claims description 47
- 238000005809 transesterification reaction Methods 0.000 claims description 36
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 32
- 239000003054 catalyst Substances 0.000 claims description 21
- -1 ethylhexyl Chemical group 0.000 claims description 19
- 238000005886 esterification reaction Methods 0.000 claims description 13
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 10
- 125000000217 alkyl group Chemical group 0.000 claims description 9
- 239000006227 byproduct Substances 0.000 claims description 4
- 125000003837 (C1-C20) alkyl group Chemical group 0.000 claims 2
- 238000006555 catalytic reaction Methods 0.000 claims 1
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 54
- 230000000052 comparative effect Effects 0.000 description 52
- 238000013508 migration Methods 0.000 description 41
- 230000005012 migration Effects 0.000 description 41
- 238000002360 preparation method Methods 0.000 description 39
- 238000006243 chemical reaction Methods 0.000 description 26
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 22
- 239000011347 resin Substances 0.000 description 22
- 229920005989 resin Polymers 0.000 description 22
- XNGIFLGASWRNHJ-UHFFFAOYSA-L phthalate(2-) Chemical compound [O-]C(=O)C1=CC=CC=C1C([O-])=O XNGIFLGASWRNHJ-UHFFFAOYSA-L 0.000 description 18
- 230000000704 physical effect Effects 0.000 description 18
- KKEYFWRCBNTPAC-UHFFFAOYSA-L terephthalate(2-) Chemical compound [O-]C(=O)C1=CC=C(C([O-])=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-L 0.000 description 13
- DOIRQSBPFJWKBE-UHFFFAOYSA-N dibutyl phthalate Chemical compound CCCCOC(=O)C1=CC=CC=C1C(=O)OCCCC DOIRQSBPFJWKBE-UHFFFAOYSA-N 0.000 description 12
- QQVIHTHCMHWDBS-UHFFFAOYSA-L isophthalate(2-) Chemical compound [O-]C(=O)C1=CC=CC(C([O-])=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-L 0.000 description 12
- NMRPBPVERJPACX-UHFFFAOYSA-N octan-3-ol Chemical compound CCCCCC(O)CC NMRPBPVERJPACX-UHFFFAOYSA-N 0.000 description 12
- 239000000376 reactant Substances 0.000 description 12
- VXUYXOFXAQZZMF-UHFFFAOYSA-N titanium(IV) isopropoxide Chemical compound CC(C)O[Ti](OC(C)C)(OC(C)C)OC(C)C VXUYXOFXAQZZMF-UHFFFAOYSA-N 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 239000002253 acid Substances 0.000 description 11
- QDTDKYHPHANITQ-UHFFFAOYSA-N 7-methyloctan-1-ol Chemical compound CC(C)CCCCCCO QDTDKYHPHANITQ-UHFFFAOYSA-N 0.000 description 9
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical group C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 9
- 238000010521 absorption reaction Methods 0.000 description 9
- 230000003247 decreasing effect Effects 0.000 description 9
- 125000004185 ester group Chemical group 0.000 description 9
- 239000007795 chemical reaction product Substances 0.000 description 8
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 8
- 229920000915 polyvinyl chloride Polymers 0.000 description 8
- 239000004800 polyvinyl chloride Substances 0.000 description 8
- YLQLIQIAXYRMDL-UHFFFAOYSA-N propylheptyl alcohol Chemical compound CCCCCC(CO)CCC YLQLIQIAXYRMDL-UHFFFAOYSA-N 0.000 description 8
- RWPICVVBGZBXNA-BGYRXZFFSA-N Bis(2-ethylhexyl) terephthalate Natural products CCCC[C@H](CC)COC(=O)C1=CC=C(C(=O)OC[C@H](CC)CCCC)C=C1 RWPICVVBGZBXNA-BGYRXZFFSA-N 0.000 description 7
- 239000004807 Di(2-ethylhexyl)terephthalate Substances 0.000 description 7
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 7
- RWPICVVBGZBXNA-UHFFFAOYSA-N bis(2-ethylhexyl) benzene-1,4-dicarboxylate Chemical compound CCCCC(CC)COC(=O)C1=CC=C(C(=O)OCC(CC)CCCC)C=C1 RWPICVVBGZBXNA-UHFFFAOYSA-N 0.000 description 7
- 238000004821 distillation Methods 0.000 description 7
- AFVFQIVMOAPDHO-UHFFFAOYSA-N Methanesulfonic acid Chemical compound CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 description 6
- BJQHLKABXJIVAM-UHFFFAOYSA-N bis(2-ethylhexyl) phthalate Chemical compound CCCCC(CC)COC(=O)C1=CC=CC=C1C(=O)OCC(CC)CCCC BJQHLKABXJIVAM-UHFFFAOYSA-N 0.000 description 6
- 230000007547 defect Effects 0.000 description 6
- 238000000605 extraction Methods 0.000 description 6
- 239000002994 raw material Substances 0.000 description 6
- 239000004439 Isononyl alcohol Substances 0.000 description 5
- WXZOXVVKILCOPG-UHFFFAOYSA-N bis(2-ethylhexyl) benzene-1,3-dicarboxylate Chemical compound CCCCC(CC)COC(=O)C1=CC=CC(C(=O)OCC(CC)CCCC)=C1 WXZOXVVKILCOPG-UHFFFAOYSA-N 0.000 description 5
- GKMYQNKPFFIGEE-UHFFFAOYSA-N bis(2-propylheptyl) benzene-1,3-dicarboxylate Chemical compound CCCCCC(CCC)COC(=O)C1=CC=CC(C(=O)OCC(CCC)CCCCC)=C1 GKMYQNKPFFIGEE-UHFFFAOYSA-N 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 230000003028 elevating effect Effects 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 239000011342 resin composition Substances 0.000 description 5
- 239000010936 titanium Substances 0.000 description 5
- VZXWJVFQXZUFQS-UHFFFAOYSA-N 4-methyl-2-propylhexan-1-ol Chemical compound CCCC(CO)CC(C)CC VZXWJVFQXZUFQS-UHFFFAOYSA-N 0.000 description 4
- QEVWDMOIPOLQBL-UHFFFAOYSA-N 5-methyl-2-propylhexan-1-ol Chemical compound CCCC(CO)CCC(C)C QEVWDMOIPOLQBL-UHFFFAOYSA-N 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 4
- 239000003377 acid catalyst Substances 0.000 description 4
- 239000012670 alkaline solution Substances 0.000 description 4
- SACPDTIKCGYPOB-UHFFFAOYSA-N bis(7-methyloctyl) benzene-1,3-dicarboxylate Chemical compound CC(C)CCCCCCOC(=O)C1=CC=CC(C(=O)OCCCCCCC(C)C)=C1 SACPDTIKCGYPOB-UHFFFAOYSA-N 0.000 description 4
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 4
- 229910001873 dinitrogen Inorganic materials 0.000 description 4
- 238000011156 evaluation Methods 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 239000012467 final product Substances 0.000 description 4
- ZSIAUFGUXNUGDI-UHFFFAOYSA-N hexan-1-ol Chemical compound CCCCCCO ZSIAUFGUXNUGDI-UHFFFAOYSA-N 0.000 description 4
- 238000006386 neutralization reaction Methods 0.000 description 4
- 238000010992 reflux Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 229910052719 titanium Inorganic materials 0.000 description 4
- UYORHVZNGJVQCF-UHFFFAOYSA-N 3-bromo-4-ethoxy-5-methoxybenzaldehyde Chemical compound CCOC1=C(Br)C=C(C=O)C=C1OC UYORHVZNGJVQCF-UHFFFAOYSA-N 0.000 description 3
- LQLQDKBJAIILIQ-UHFFFAOYSA-N Dibutyl terephthalate Chemical compound CCCCOC(=O)C1=CC=C(C(=O)OCCCC)C=C1 LQLQDKBJAIILIQ-UHFFFAOYSA-N 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 230000000996 additive effect Effects 0.000 description 3
- DPOVUUGVOSHDAT-UHFFFAOYSA-N benzene-1,3-dicarboxylic acid;phthalic acid;terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1.OC(=O)C1=CC=CC(C(O)=O)=C1.OC(=O)C1=CC=CC=C1C(O)=O DPOVUUGVOSHDAT-UHFFFAOYSA-N 0.000 description 3
- MTYUOIVEVPTXFX-UHFFFAOYSA-N bis(2-propylheptyl) benzene-1,2-dicarboxylate Chemical compound CCCCCC(CCC)COC(=O)C1=CC=CC=C1C(=O)OCC(CCC)CCCCC MTYUOIVEVPTXFX-UHFFFAOYSA-N 0.000 description 3
- 239000012159 carrier gas Substances 0.000 description 3
- 230000006866 deterioration Effects 0.000 description 3
- HBGGXOJOCNVPFY-UHFFFAOYSA-N diisononyl phthalate Chemical compound CC(C)CCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCC(C)C HBGGXOJOCNVPFY-UHFFFAOYSA-N 0.000 description 3
- 238000009408 flooring Methods 0.000 description 3
- 238000004817 gas chromatography Methods 0.000 description 3
- 239000001307 helium Substances 0.000 description 3
- 229910052734 helium Inorganic materials 0.000 description 3
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 3
- 229940098779 methanesulfonic acid Drugs 0.000 description 3
- 239000012299 nitrogen atmosphere Substances 0.000 description 3
- 235000012424 soybean oil Nutrition 0.000 description 3
- 239000003549 soybean oil Substances 0.000 description 3
- 239000003381 stabilizer Substances 0.000 description 3
- 239000003981 vehicle Substances 0.000 description 3
- AUZOVTCTIDMGEW-LKUWHMJMSA-N (2r)-2-[[2-[[(2s)-4-amino-2-[[(2s)-2-[[(2s)-2-[[(2s)-1-[(2s)-2-amino-4-methylpentanoyl]pyrrolidine-2-carbonyl]amino]propanoyl]amino]-3-[(2r,4s)-5,5-dimethyl-2-[[(2-phenylacetyl)amino]methyl]-1,3-thiazolidine-4-carbonyl]oxypropanoyl]amino]-4-oxobutanoyl]am Chemical compound CC(C)C[C@H](N)C(=O)N1CCC[C@H]1C(=O)N[C@@H](C)C(=O)N[C@H](C(=O)N[C@@H](CC(N)=O)C(=O)NCC(=O)N[C@H](C(C)C)C(O)=O)COC(=O)[C@H]1C(C)(C)S[C@H](CNC(=O)CC=2C=CC=CC=2)N1 AUZOVTCTIDMGEW-LKUWHMJMSA-N 0.000 description 2
- KBPLFHHGFOOTCA-UHFFFAOYSA-N 1-Octanol Chemical compound CCCCCCCCO KBPLFHHGFOOTCA-UHFFFAOYSA-N 0.000 description 2
- KPWZIBLNIHZJLB-UHFFFAOYSA-N 1-o-butyl 4-o-(2-ethylhexyl) benzene-1,4-dicarboxylate Chemical compound CCCCOC(=O)C1=CC=C(C(=O)OCC(CC)CCCC)C=C1 KPWZIBLNIHZJLB-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- 150000004703 alkoxides Chemical class 0.000 description 2
- CRPXFUDVZZLWAP-UHFFFAOYSA-N bis(8-methylnonyl) benzene-1,3-dicarboxylate Chemical compound CC(C)CCCCCCCOC(=O)C1=CC=CC(C(=O)OCCCCCCCC(C)C)=C1 CRPXFUDVZZLWAP-UHFFFAOYSA-N 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- MWKFXSUHUHTGQN-UHFFFAOYSA-N decan-1-ol Chemical compound CCCCCCCCCCO MWKFXSUHUHTGQN-UHFFFAOYSA-N 0.000 description 2
- 210000000750 endocrine system Anatomy 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000005556 hormone Substances 0.000 description 2
- 229940088597 hormone Drugs 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 125000004108 n-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 2
- ZWRUINPWMLAQRD-UHFFFAOYSA-N nonan-1-ol Chemical compound CCCCCCCCCO ZWRUINPWMLAQRD-UHFFFAOYSA-N 0.000 description 2
- 125000002524 organometallic group Chemical group 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- AUEOCOKTCYDEAZ-UHFFFAOYSA-N 1-O-butyl 4-O-(2-propylheptyl) benzene-1,4-dicarboxylate Chemical compound C(C1=CC=C(C(=O)OCC(CCCCC)CCC)C=C1)(=O)OCCCC AUEOCOKTCYDEAZ-UHFFFAOYSA-N 0.000 description 1
- QRZRUIUKACJNLQ-UHFFFAOYSA-N 1-O-butyl 4-O-(7-methyloctyl) benzene-1,4-dicarboxylate Chemical compound C(C1=CC=C(C(=O)OCCCCCCC(C)C)C=C1)(=O)OCCCC QRZRUIUKACJNLQ-UHFFFAOYSA-N 0.000 description 1
- AWFYPPSBLUWMFQ-UHFFFAOYSA-N 2-[5-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]-1,3,4-oxadiazol-2-yl]-1-(1,4,6,7-tetrahydropyrazolo[4,3-c]pyridin-5-yl)ethanone Chemical group C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C1=NN=C(O1)CC(=O)N1CC2=C(CC1)NN=C2 AWFYPPSBLUWMFQ-UHFFFAOYSA-N 0.000 description 1
- YIWUKEYIRIRTPP-UHFFFAOYSA-N 2-ethylhexan-1-ol Chemical compound CCCCC(CC)CO YIWUKEYIRIRTPP-UHFFFAOYSA-N 0.000 description 1
- ALKCLFLTXBBMMP-UHFFFAOYSA-N 3,7-dimethylocta-1,6-dien-3-yl hexanoate Chemical compound CCCCCC(=O)OC(C)(C=C)CCC=C(C)C ALKCLFLTXBBMMP-UHFFFAOYSA-N 0.000 description 1
- AZIIFCSXYZNYCA-UHFFFAOYSA-N 3-O-octan-3-yl 1-O-(2-propylheptyl) benzene-1,3-dicarboxylate Chemical compound C(C1=CC(C(=O)OC(CCCCC)CC)=CC=C1)(=O)OCC(CCCCC)CCC AZIIFCSXYZNYCA-UHFFFAOYSA-N 0.000 description 1
- GPZYYYGYCRFPBU-UHFFFAOYSA-N 6-Hydroxyflavone Chemical compound C=1C(=O)C2=CC(O)=CC=C2OC=1C1=CC=CC=C1 GPZYYYGYCRFPBU-UHFFFAOYSA-N 0.000 description 1
- WTFUTSCZYYCBAY-SXBRIOAWSA-N 6-[(E)-C-[[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]piperazin-1-yl]methyl]-N-hydroxycarbonimidoyl]-3H-1,3-benzoxazol-2-one Chemical group C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)N1CCN(CC1)C/C(=N/O)/C1=CC2=C(NC(O2)=O)C=C1 WTFUTSCZYYCBAY-SXBRIOAWSA-N 0.000 description 1
- PLLBRTOLHQQAQQ-UHFFFAOYSA-N 8-methylnonan-1-ol Chemical compound CC(C)CCCCCCCO PLLBRTOLHQQAQQ-UHFFFAOYSA-N 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- 102100035474 DNA polymerase kappa Human genes 0.000 description 1
- 101710108091 DNA polymerase kappa Proteins 0.000 description 1
- ZVFDTKUVRCTHQE-UHFFFAOYSA-N Diisodecyl phthalate Chemical compound CC(C)CCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCCC(C)C ZVFDTKUVRCTHQE-UHFFFAOYSA-N 0.000 description 1
- 239000004440 Isodecyl alcohol Substances 0.000 description 1
- 229920001944 Plastisol Polymers 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
- WNLRTRBMVRJNCN-UHFFFAOYSA-L adipate(2-) Chemical compound [O-]C(=O)CCCCC([O-])=O WNLRTRBMVRJNCN-UHFFFAOYSA-L 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- SAOKZLXYCUGLFA-UHFFFAOYSA-N bis(2-ethylhexyl) adipate Chemical compound CCCCC(CC)COC(=O)CCCCC(=O)OCC(CC)CCCC SAOKZLXYCUGLFA-UHFFFAOYSA-N 0.000 description 1
- ORTYRKBSNXTIFO-UHFFFAOYSA-N bis(2-propylheptyl) benzene-1,4-dicarboxylate Chemical compound CCCCCC(CCC)COC(=O)C1=CC=C(C(=O)OCC(CCC)CCCCC)C=C1 ORTYRKBSNXTIFO-UHFFFAOYSA-N 0.000 description 1
- PEIIRIVDOVFUIW-UHFFFAOYSA-N bis(7-methyloctyl) benzene-1,4-dicarboxylate Chemical compound CC(C)CCCCCCOC(=O)C1=CC=C(C(=O)OCCCCCCC(C)C)C=C1 PEIIRIVDOVFUIW-UHFFFAOYSA-N 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000003490 calendering Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000007580 dry-mixing Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000002649 leather substitute Substances 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 239000004999 plastisol Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000565 sealant Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C69/00—Esters of carboxylic acids; Esters of carbonic or haloformic acids
- C07C69/76—Esters of carboxylic acids having a carboxyl group bound to a carbon atom of a six-membered aromatic ring
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C69/00—Esters of carboxylic acids; Esters of carbonic or haloformic acids
- C07C69/76—Esters of carboxylic acids having a carboxyl group bound to a carbon atom of a six-membered aromatic ring
- C07C69/80—Phthalic acid esters
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
- C07B61/00—Other general methods
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/03—Preparation of carboxylic acid esters by reacting an ester group with a hydroxy group
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/08—Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/48—Separation; Purification; Stabilisation; Use of additives
- C07C67/52—Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation
- C07C67/54—Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation by distillation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C69/00—Esters of carboxylic acids; Esters of carbonic or haloformic acids
- C07C69/76—Esters of carboxylic acids having a carboxyl group bound to a carbon atom of a six-membered aromatic ring
- C07C69/80—Phthalic acid esters
- C07C69/82—Terephthalic acid esters
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/18—Plasticising macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/0008—Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
- C08K5/0016—Plasticisers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/10—Esters; Ether-esters
- C08K5/12—Esters; Ether-esters of cyclic polycarboxylic acids
Definitions
- the present invention relates to an ester compound, an ester composition including the same, a preparation method of the plasticizer composition and a resin composition including the plasticizer composition as a plasticizer, and more particularly, to an ester composition including three kinds of isophthalate-based compounds, a preparation method of the plasticizer composition and a resin composition including the plasticizer composition as a plasticizer.
- a plasticizer is a corresponding ester obtained by the reaction of an alcohol with a polycarboxylic acid such as phthalic acid and adipic acid.
- a polycarboxylic acid such as phthalic acid and adipic acid.
- Commercially significant examples include an adipate of C8, C9 and C10 alcohol such as di(2-ethylhexyl) adipate, diisononyl adipate and diisodecyl adipate; and a phthalate of C8, C9 and C10 alcohol such as di(2-ethylhexyl) phthalate, diisononyl phthalate and diisodecyl phthalate.
- the di(2-ethylhexyl) phthalate is used for manufacturing plastisol and a toy, a film, shoes, a paint, a flooring material, gloves, a wall paper, a synthetic leather, a sealant, tarpaulin, a coating agent of the bottom of a vehicle, a furniture, a foamed mat and a soundproof panel via a dry mixing, and may be used for manufacturing an outer packing and insulation of a PVC cable, and for producing other calendered PVC products with plasticity.
- di-(2-ethylhexyl) phthalate, etc. are widely used as an ester-based plasticizer, however these compounds are environmental hormones disturbing endocrine system and are harmful to a human body, and have a limit in improving the processability of a resin, absorption rate with a resin, the degree of migration loss and heat stability.
- a technical task intended to be solved in the present invention is to provide a novel ester-based compound.
- Another technical task to be solved in the present invention is to provide an ester-based composition having good plasticizing efficiency and improved processability of a resin and providing good physical properties when prescribing a sheet and a compound such as a cable, an interior material of a vehicle, a film, a sheet, a tube, a wall paper, a toy, a flooring material, etc.
- Another technical task to be solved in the present invention is to provide a preparation method of the ester-based composition.
- Final technical task to be solved in the present invention is to provide a resin composition including the ester-based composition as a plasticizer.
- an ester composition which is a plasticizer, the composition including the compounds of the following Formula 1, Formula 2 and Formula 3.
- R 1 is C3-C5 non-branch type alkyl
- R 2 is C6-C12 branch-type alkyl
- R 1 C3-C5 non-branch type alkyl
- R 2 is C6-C12 branch-type alkyl
- ester-based compound selected from the group consisting of compounds of the following formulae.
- the ester compound according to an embodiment of the present invention improves plasticization efficiency and the processability of a resin when used as a plasticizer, and provides good physical properties such as tensile strength, elongation rate, migration resistance, volatile loss, etc.
- an ester-based composition including the following Formula 1, Formula 2 and Formula 3 is provided. as defined in claim 1.
- the ester composition includes an isophthalate-based ester compound in which ester groups (-COO-) are present at positions 1 and 3 in a benzene ring, that is, at a meta position, is more eco-friendly, has better physical properties including tensile strength, elongation rate, migration loss, volatile loss, etc., and has good processability and workability of a product when compared to a phthalate-based ester compound having ester groups (-COO-) at other positions, for example, an ortho position (positions 1 and 2 in a benzene ring) or a para position (positions 1 and 4 in a benzene ring).
- a phthalate-based compound in which ester groups are present at an ortho position is an environmental hormone disturbing endocrine system and harmful to a human body, and have a limit in improving the processability of a resin, absorption rate with a resin, the degree of migration loss, and heat stability.
- terephthalate-based ester compound having ester groups at para position has relatively deteriorated compatibility and combination stability with the resin due to the linear structure thereof, and these defects may be adversely affecting factors to the processability and workability of a product.
- ester-based compound according to an embodiment of the present invention as the plasticizer of the resin composition, equivalent tensile strength and elongation rate may be secured when compared to a common phthalate-based compound widely used as a plasticizer.
- volatile loss may be decreased, and migration resistance may be markedly excellent.
- a compound in which R 1 is a non-branch type, and R 2 is a branch type may have improved hardness, tensile strength and elongation rate when compared to a compound in which both R 1 and R 2 have a branch type or a non-branch type.
- the productivity and processability of a final product may be improved due to the improved tensile strength and elongation rate.
- R 2 may be selected from ethylhexyl, isononyl, and propylheptyl.
- the present invention may provide an ester-based compound of the following formulae.
- the ester compounds of the following formulae may be hybrid type compounds.
- the ester-based composition may include the compounds of the following Formulae 1-1, 2-1 and 3-1.
- the ester-based composition may include the compounds of the following Formulae 1-1, 2-2 and 3-2.
- the ester-based composition may include the compounds of the following Formulae 1-1, 2-3 and 3-3.
- the ester-based composition may include the compounds of the following Formulae 1-1, 2-4 and 3-4.
- the compounds of Formula 1, Formula 2 and Formula 3 may be included in an amount ratio of 0.5 to 50 wt%, 0.5 to 70 wt% and 0.5 to 85 wt% with respect to the total amount of the ester composition, respectively, and particularly, in an amount ratio of 0.5 to 50 wt%, 10 to 50 wt% and 35 to 80 wt%.
- the mixing ratio of the total amount of the non-hybrid type compounds of Formulae 1 and 3 and the hybrid type compound of Formula 2 may be 95:5 to 30:70, and preferably, 90:10 to 60:40 by weight.
- the ester-based composition includes the isophthalate-based compounds of Formulae 1 to 3 in the above-described specific amount range and so, is eco-friendly and has short absorption rate and short melting time with respect to a resin to improve the processability of the resin.
- physical properties such as hardness, tensile strength, elongation rate, migration loss, sheet volatile loss, heat stability, QUV, etc. may be further improved.
- the ester-based composition according to an embodiment of the present invention may be an ether-free plasticizer, and in this case, plasticizing efficiency is good, and workability is good.
- Ether-free composition means an ester-based composition in which an ether component included in the composition is 1,000 ppm and less, 100 ppm and less, or 10 ppm and less.
- a preparation method of the ester-based composition including conducting a trans-esterification reaction of a compound of the following Formula 3 with a first alcohol of the following Formula 4.
- trans-esterification reaction used in the present invention means a reaction is conducted between an alcohol and an ester as in the following Reaction 1, and R" of the ester and R' of the alcohol are interchanged.
- the compound of Formula 1 may be produced when the alkoxide of the first alcohol of Formula 4 attacks two carbon atoms of the ester group (RCOOR") of the compound of Formula 3, the compound of Formula 2 may be produced when the alkoxide attacks one carbon atom of the ester group (RCOOR") of the compound of Formula 3, and the compound of Formula 3 may remain as an unreacted part.
- the trans-esterification reaction may not induce defects concerning waste water when compared to an esterification reaction between acid-alcohol, and may not induce defects generated when using an acid catalyst because the trans-esterification reaction may be conducted without a catalyst.
- the compound of Formula 1, the compound of Formula 2 and the compound of Formula 3 may be produced in an amount of 0.5 to 50 wt%, 0.5 to 70 wt% and 0.5 to 85 wt%, respectively, with respect to the total amount of the ester-based composition, and particularly in an amount of 0.5 to 50 wt%, 10 to 50 wt% and 35 to 80 wt%.
- an ester-based composition having high process efficiency as a plasticizer and having good processability and absorption rate may be obtained.
- the ester-based composition prepared by the trans-esterification reaction may include all of the compound of Formula 1, the compound of Formula 2 and the compound of Formula 3, and the composition of the ester-based composition may be controlled according to the amount added of the first alcohol of Formula 4.
- the amount added of the first alcohol of Formula 4 may be 0.1 to 89.9 parts by weight, particularly, 3 to 50 parts by weight, and more particularly, 5 to 40 parts by weight with respect to 100 parts by weight of the compound of Formula 3.
- the mole fraction of the compound of Formula 3 participating in the trans-esterification reaction may be increased, and the amount of the compound of Formula 1 and the compound of Formula 2 may be increased in the ester-based composition.
- the amount of the unreacted compound of Formula 3 may be decreased correspondingly.
- the molar ratio of the compound of Formula 3 and the first alcohol of Formula 4 may be, for example, 1 : 0.005 to 5.0, 1 : 0.05 to 2.5, or 1 : 0.1 to 1.0, and in this range, an ester-based composition having high process efficiency and processability improving effects may be obtained.
- the trans-esterification reaction may preferably be conducted under the reaction temperature of 120°C to 190°C, preferably 135°C to 180°C, and more preferably, 141°C to 179°C, for from 10 minutes to 10 hours, preferably from 30 minutes to 8 hours, and more preferably from 1 to 6 hours.
- the reaction time may be calculated after elevating the temperature from the time of attainment of the reaction temperature.
- the trans-esterification reaction may be conducted in the presence of an acid catalyst or a metal catalyst, and in this case, the reaction time may be decreased.
- the acid catalyst may be sulfuric acid, methanesulfonic acid, p-toluenesulfonic acid, etc.
- the metal catalyst may be an organometallic catalyst, a metal oxide catalyst, a metal salt catalyst, a metal itself, etc.
- the metal component may be at least one selected from the group consisting of tin, titanium and zirconium, or a mixture of at least two thereof.
- a removing process for removing the unreacted alcohol and reaction by-products for example, the compound of Formula 3 by distillation may be further included after conducting the trans-esterification reaction.
- the distillation may be, for example, two-step distillation for separating the first alcohol of Formula 4 from the by-products using the difference between boiling points thereof.
- the distillation may be mixed distillation.
- the ester-based composition may be relatively stably secured with desired composition.
- the mixed distillation means the distillation of butanol and the by-products at the same time.
- the compound of Formula 3 used in the trans-esterification reaction of the present invention may be obtained by conducting an esterification reaction of the compound of the following Formula 5 with the second alcohol of the following Formula 6 or a mixture of the second alcohol with at least one isomer thereof in the presence of a catalyst.
- R 2 is alkyl of C 1 -C 20 .
- the esterification reaction may be conducted under the reaction temperature of 80°C to 270°C, preferably 150°C to 250°C, for from 10 minutes to 10 hours, preferably from 30 minutes to 8 hours, and more preferably from 1 to 6 hours. Within the temperature range and the time period range, the compound of Formula 1 may be effectively obtained.
- the catalyst used in the esterification reaction may be an organometallic catalyst including a Sn-based or a Ti-based catalyst, an acid catalyst including a sulfonic acid-based or a sulfuric-based catalyst, or a mixture catalyst thereof, and the kind of the catalyst is not limited.
- the compound of Formula 5 and the second alcohol of Formula 6 may be used in a molar ratio of 1 : 1 to 7, and preferably, 1 : 2 to 5.
- the second alcohol of the above Formula 6 may be used by preparing a common method or may be available on the market.
- the second alcohol of the above Formula 6 may be included as a mixture with at least one isomer thereof, and the amount of the second alcohol of Formula 6 : the isomer thereof may be, for example, 50 to 100 parts by weight : 0 to 50 parts by weight, and preferably 70 to 100 parts by weight : 0 to 30 parts by weight.
- the second alcohol of the above Formula 6 or the mixture of the second alcohol and the isomer thereof may be commercially available.
- 2-propylheptane-1-ol CAS No. 10042-59-8 , 66256-62-0, 159848-27-8, etc. of BASF Co. including the isomer thereof may be purchased and used
- isononyl alcohol CAS No. 68526-84-1 of EXXONMOBILE Co., CAS No. 27458-94-2 (68515-81-1) of KYOWA Co., etc. including the isomer thereof may be purchased and used.
- the present invention is not limited thereto.
- the ester-based composition according to an embodiment of the present invention may further include the compound of the above Formulae 1 to 3, preferably the compound of Formulae 2 and 3 may further include the isomer thereof, respectively.
- the compound of Formula 3 may be prepared with the yield of about 80% and over.
- the ester-based composition having a desired composition may be easily prepared.
- the present invention provides an ester-based composition prepared by the above preparation method.
- the ester-based composition according to an embodiment of the present invention has short absorption rate and short melting time with respect to the resin, and the processability of the resin may be improved, and good physical properties may be provided when prescribing a sheet and a compound such as a cable, an interior material of a vehicle, a film, a sheet, a tube, a wall paper, a toy, a flooring material, etc.
- distillation-extraction under a reduced pressure was conducted for 0.5 to 4 hours to remove unreacted raw materials.
- steam extraction was conducted using steam under a reduced pressure for 0.5 to 3 hours.
- the temperature of the reactant was lowered to about 90°C, and neutralization treatment was conducted using an alkaline solution.
- washing may be conducted, followed by dehydrating the reactant to remove water.
- a filter medium was inserted to the dehydrated reactant, followed by stirring for a certain time and filtering to finally obtain 1,162 g of di-(2-ethylhexyl) isophthalate (yield 99.0%).
- Bis-(2-propylheptyl) isophthalate was obtained by conducting the same procedure described in Preparation Example 1 except for using 2-propylheptyl alcohol (2-propylheptane-1-ol (85-100 %), 1-hexanol; 4-methyl-2-propyl (0-15%); 1-hexanol, 5-methyl-2-propyl (0-15%)) ( CAS No. 10042-59-8, 66256-62-0 and 159848-27-8 of BASF Co.) instead of ethylhexyl alcohol.
- Bis(isononyl) isophthalate was obtained by conducting the same procedure described in Preparation Example 1 except for using isononyl alcohol ( CAS No. 68526-84-1 of EXXONMOBILE Co.) instead of ethylhexyl alcohol.
- Bis(isodecyl) isophthalate was obtained by conducting the same procedure described in Preparation Example 1 except for using isodecyl alcohol instead of ethylhexyl alcohol.
- the reaction product was mixed distilled to remove butanol and 2-ethylhexyl alcohol and to finally prepare an ester-based composition.
- Ester-based compositions having the composition of the compounds of Formula 1, Formula 2 and Formula 3 were obtained by conducting the same procedure described in Example 1 except for controlling the amount of the butanol as described in the following Table 1.
- distillation-extraction under a reduced pressure was conducted for 0.5 to 4 hours to remove unreacted raw materials.
- steam extraction was conducted using steam under a reduced pressure for 0.5 to 3 hours.
- the temperature of the reactant was lowered to about 90°C, and neutralization treatment was conducted using an alkaline solution. In addition, washing may be conducted, followed by dehydrating the reactant to remove water.
- a filter medium was inserted to the dehydrated reactant, followed by stirring for a certain time and filtering to finally obtain 2 wt% of DEHIP, 25 wt% of 2-propylheptyl ethylhexyl isophthalate (PHEHIP) and 73 wt% of bis(2-propylheptyl) isophthalate (DPHIP).
- DEHIP 2-propylheptyl ethylhexyl isophthalate
- DPHIP bis(2-propylheptyl) isophthalate
- a reaction product including 75.5 wt% of di-(2-ethylhexyl) terephthalate (DEHTP), 22.8 wt% of 1-butyl 4-(2-ethylhexyl) terephthalate (hereinafter, BEHTP) and 1.7 wt% of dibutyl terephthalate (hereinafter, DBTP) was obtained by conducting the same procedure described in Preparation Example 1 and Example 1 using terephthalic acid instead of isophthalic acid prepared in Preparation Example 1.
- a reaction product including 75.0 wt% of di-(2-ethylhexyl) terephthalate (DEHP), 22.5 wt% of 1-butyl 4-(2-ethylhexyl) terephthalate (hereinafter, BEHP) and 2.5 wt% of dibutyl phthalate (hereinafter, DBP) was obtained by conducting the same procedure described in Preparation Example 1 and Example 1 using phthalic acid instead of isophthalic acid prepared in Preparation Example 1.
- Example 1 Butanol amount (parts by weight) Formula 1 (wt%) Formula 2 (wt%) Formula 3 (wt%)
- Example 1 7 parts by weight (Formula 1-1) 1.5 (Formula 2-1) 22.4 (Formula 3-1) 76.1
- Example 2 7 parts by weight (Formula 1-1) 1.4 (Formula 2-2) 20.7 (Formula 3-2) 77.9
- Example 3 7 parts by weight (Formula 1-1) 1.5 (Formula 2-3) 21.3 (Formula 3-3) 77.2
- Example 4 (1P) 7 parts by weight (Formula 1-1) 1.4 (Formula 2-4) 20.5 (Formula 3-4) 78.1
- Example 5 (1P) 4 parts by weight (Formula 1-1) 0.6 (Formula 2-1) 14.4 (Formula 3-1) 85.0
- Example 6 10 parts by weight (Formula 1-1) 2.8 (Formula 2-1) 28.4 (Formula 3-1) 68.8
- Example 7 13 parts by weight (Formula 1-1) 13 parts
- ester-based compositions prepared in Examples 1 to 13 and Comparative Examples 1 to 3 55 parts by weight of a plasticizer, 2 parts by weight of a BZ stabilizer (BZ210, Songwon Industries) as an additive and 2 parts by weight of an epoxidized soybean oil (ESO, Songwon Industries) with respect to 100 parts by weight of a polyvinyl chloride resin (PVC, LS 130s) were mixed in a rotational rate of 1,300 rpm at 100°C.
- a process was conducted using a roll mill at 175 for 4 minutes and using a press at 185°C for 3 minutes (low pressure) and for 2 minutes and 30 seconds (high pressure) to manufacture a sheet to a thickness of 2 mm.
- Shore hardness (Shore A) at 25°C was measured using ASTM D2240.
- the ester-based compositions of Examples 1 to 4 of the present invention prepared by the trans-esterification reaction have markedly improved hardness, tensile strength and elongation rate when compared to those of the ester-based composition of Comparative Example 1.
- the ester-based compositions of Examples 1 to 4 of the present invention particularly, the ester-based compositions of Examples 1 to 4 in which R 1 is a non-branch type, and R 2 is a branch type by the trans-esterification reaction have better hardness, tensile strength and elongation rate when compared to the ester-based composition of Comparative Example 1 in which both R 1 and R 2 have a branch type.
- the hardness of the ester-based compositions of Examples 1 to 4 is decreased by 5% and over when compared to the ester-based composition of Comparative Example 1. Since the hardness is decreased as in the examples of the present invention, good processability and the stabilization of workability may be provided when applied in a practical product.
- Table 3 shows the hardness, tensile strength, elongation rate and migration resistance of the ester-based compositions of Examples 5 to 13 according to the amount added of butanol.
- the hardness, tensile strength and elongation rate are relatively improved while the migration resistance is decreased according to the decrease of the amount added of butanol.
- Table 4 shows the results of the hardness, tensile strength, elongation rate and migration resistance of the sheets manufactured using the plasticizers of Example 1 and Comparative Examples 2 and 3 by changing the kinds of an acid.
- the elongation rate is improved, and the effects of migration resistance and volatile loss are good for the ester-based compositions of the examples of the present invention using an isophthalate-based ester plasticizers when compared to the ester-based compositions of Comparative Examples 2 and 3 using terephthalate-based and phthalate-based ester plasticizers.
- the elongation rate, migration resistance and volatile loss are improved when compared to the phthalate-based and terephthalate-based ester plasticizer having ester groups at ortho position and para position.
- the processability of a resin, absorption rate with the resin, the degree of migration loss and heat stability are improved.
- the migration resistance of the specimen of Example 1 of the present invention may be decreased 10 times and less when compared to that of Comparative Example 3.
- the volatile loss of the specimen of Example 1 of the present invention may decrease to about 20 to 45% when compared to that of Comparative Examples 2 and 3.
- the decrease of the volatile loss as in Comparative Examples 2 and 3 may be a fatal defect in the processability and the stability for a long time of a final product. That is, the increase of the volatile loss means the decrease of the amount of the ester-based composition (plasticizer) present in the specimen and the deterioration of the elongation rate.
- the physical properties of the isophthalate-based ester plasticizer of the present invention are markedly increased when compared to a terephthalate-based and phthalate-based plasticizers.
- DPHIP di-(2-propylheptyl) isophthalate
- Ester-based compositions having the compositions of Formula 2-2, Formula 1-1 and Formula 3-2 in the following Table 5 were obtained by conducting the same procedure described in Example 14 except for controlling the amount of butanol as described in the following Table 5.
- a reaction product including 75.4 wt% of di-(2-propylheptyl) terephthalate (DPHTP), 23.2 wt% of 1-butyl 4-(2-propylheptyl) terephthalate (hereinafter, BPHTP) and 1.4 wt% of dibutyl terephthalate (hereinafter, DBTP) was obtained by conducting the same procedure described in Preparation Example 2 and Example 14 using terephthalic acid instead of isophthalic acid prepared in Preparation Example 2.
- a reaction product including 74.5 wt% of di-(2-propylheptyl) phthalate (DPHP), 22.1 wt% of 1-butyl 4-(2-propylheptyl) phthalate (hereinafter, BPHP) and 3.4 wt% of dibutyl phthalate (hereinafter, DBP) was obtained by conducting the same procedure described in Preparation Example 2 and an example using phthalic acid instead of isophthalic acid prepared in Preparation Example 2.
- ester-based composition prepared in Examples 14 to 21 and Comparative Examples 3 to 5 55 parts by weight of a plasticizer, 2 parts by weight of a BZ stabilizer (BZ210, Songwon Industries) as an additive and 2 parts by weight of an epoxidized soybean oil (ESO, Songwon Industries) with respect to 100 parts by weight of a polyvinyl chloride resin
- Table 6 shows the hardness, tensile strength, elongation rate and migration resistance of the ester-based compositions of Examples 15 to 21 according to the amount added of butanol.
- the hardness, tensile strength and elongation rate are relatively improved while the migration resistance is decreased according to the decrease of the amount added of butanol.
- the physical properties may be controlled according to use by controlling the amount of butanol, and it would be secured that the ester-based compositions may be usefully applied.
- Table 7 shows the results of the hardness, tensile strength, elongation rate and migration resistance of the sheets manufactured using the plasticizers of Example 14 and Comparative Examples 4 and 5 by changing the kinds of an acid.
- the elongation rate, migration resistance and volatile loss are improved when compared to the phthalate-based and terephthalate-based ester plasticizer having ester groups at ortho position and para position.
- the processability of a resin, absorption rate with the resin, the degree of migration loss and heat stability are improved.
- the volatile loss of the specimen of Example 14 of the present invention may decrease to about 30 to 65% when compared to that of Comparative Examples 4 and 5.
- the increase of the volatile loss as in Comparative Examples 4 and 5 may be a fatal defect in the processability and the stability for a long time of a final product. That is, the increase of the volatile loss means the decrease of the amount of the ester-based composition (plasticizer) present in the specimen and the deterioration of the elongation rate.
- the physical properties of the isophthalate-based ester plasticizer of the present invention be markedly increased when compared to those of a terephthalate-based and phthalate-based plasticizers.
- Ester-based compositions having the compositions of Formula 2-3, Formula 1-1 and Formula 3-3 in the following Table 8 were obtained by conducting the same procedure described in Example 22 except for controlling the amount of butanol as described in the following Table 8.
- a reaction product including 75.1 wt% of di-(isononyl) terephthalate (DINTP), 23.0 wt% of 1-butyl 4-(isononyl) terephthalate (hereinafter, BINTP) and 1.9 wt% of dibutyl terephthalate (hereinafter, DBTP) was obtained by conducting the same procedure described in Preparation Example 3 and Example 22 using terephthalic acid instead of isophthalic acid prepared in Preparation Example 3.
- a reaction product including 75.9 wt% of di-(isononyl) phthalate (DNIP), 22.0 wt% of 1-butyl 4-(isononyl) phthalate (hereinafter, BINP) and 2.1 wt% of dibutyl phthalate (hereinafter, DBP) was obtained by conducting the same procedure described in Preparation Example 3 and Example 22 using phthalic acid instead of isophthalic acid prepared in Preparation Example 3.
- BZ210 BZ210, Songwon Industries
- EEO epoxidized soybean oil
- Table 9 shows the hardness, tensile strength, elongation rate and migration resistance of the ester-based compositions of Examples 23 to 29 according to the amount added of butanol.
- the hardness, tensile strength and elongation rate are relatively improved while the migration resistance is decreased according to the decrease of the amount added of butanol.
- the physical properties may be controlled according to use by controlling the amount of butanol, and it may be secured that the ester-based compositions may be usefully applied.
- Example/Comparative example Example 22 Comparative Example 6 Comparative Example 7 Acid Isophthalic acid Terephthalic acid Phthalic acid Reaction Trans-esterification Trans-esterification Trans-esterification Physical properties Hardness (Shore A) 88.5 89.5 88.3 Tensile strength (kg/cm 2 ) 225.7 254.6 220.9 Elongation rate (%) 290.6 240.8 284.3 Migration loss (%) 0.05 0.09 0.04 Volatile loss (%) 1.02 1.45 1.23
- Table 10 shows the results of the hardness, tensile strength, elongation rate and migration resistance of the sheets manufactured using the plasticizers of Example 22 and Comparative Examples 6 and 7 by changing the kinds of an acid.
- the elongation rate is improved, and the effects of migration resistance and volatile loss are good for the ester-based composition of the example of the present invention using an isophthalate-based ester plasticizer when compared to the ester-based compositions of Comparative Examples 6 and 7 using terephthalate-based and phthalate-based ester plasticizers.
- the elongation rate, migration resistance and volatile loss are improved when compared to the phthalate-based and terephthalate-based ester plasticizer having ester groups at ortho position and para position.
- the processability of a resin, absorption rate with the resin, the degree of migration loss and heat stability are improved.
- the volatile loss of the specimen of Example 22 of the present invention may decrease to about 20 to 45% when compared to that of Comparative Examples 6 and 7.
- the increase of the volatile loss as in Comparative Examples 6 and 7 may be a fatal defect in the processability and the stability for a long time of a final product. That is, the increase of the volatile loss means the decrease of the amount of the ester-based composition (plasticizer) present in the specimen and the deterioration of the elongation rate.
- the physical properties of the isophthalate-based ester plasticizer composition of the present invention may be markedly increased when compared to a terephthalate-based and phthalate-based plasticizers.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Crystallography & Structural Chemistry (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Description
- The present invention relates to an ester compound, an ester composition including the same, a preparation method of the plasticizer composition and a resin composition including the plasticizer composition as a plasticizer, and more particularly, to an ester composition including three kinds of isophthalate-based compounds, a preparation method of the plasticizer composition and a resin composition including the plasticizer composition as a plasticizer.
- Generally, a plasticizer is a corresponding ester obtained by the reaction of an alcohol with a polycarboxylic acid such as phthalic acid and adipic acid. Commercially significant examples include an adipate of C8, C9 and C10 alcohol such as di(2-ethylhexyl) adipate, diisononyl adipate and diisodecyl adipate; and a phthalate of C8, C9 and C10 alcohol such as di(2-ethylhexyl) phthalate, diisononyl phthalate and diisodecyl phthalate.
- Particularly, the di(2-ethylhexyl) phthalate is used for manufacturing plastisol and a toy, a film, shoes, a paint, a flooring material, gloves, a wall paper, a synthetic leather, a sealant, tarpaulin, a coating agent of the bottom of a vehicle, a furniture, a foamed mat and a soundproof panel via a dry mixing, and may be used for manufacturing an outer packing and insulation of a PVC cable, and for producing other calendered PVC products with plasticity.
- Now, di-(2-ethylhexyl) phthalate, etc. are widely used as an ester-based plasticizer, however these compounds are environmental hormones disturbing endocrine system and are harmful to a human body, and have a limit in improving the processability of a resin, absorption rate with a resin, the degree of migration loss and heat stability.
- Thus, the development on an ester compound which is eco-friendly, sufficiently improves all physical properties including the processability of a resin, the absorption rate with a resin, the degree of migration loss, heat stability, etc., and a method of preparing the same is required.
- A technical task intended to be solved in the present invention is to provide a novel ester-based compound.
- Another technical task to be solved in the present invention is to provide an ester-based composition having good plasticizing efficiency and improved processability of a resin and providing good physical properties when prescribing a sheet and a compound such as a cable, an interior material of a vehicle, a film, a sheet, a tube, a wall paper, a toy, a flooring material, etc.
- Another technical task to be solved in the present invention is to provide a preparation method of the ester-based composition.
- Final technical task to be solved in the present invention is to provide a resin composition including the ester-based composition as a plasticizer.
-
- In the above Formulae 1 to 3, R1 is C3-C5 non-branch type alkyl, and R2 is C6-C12 branch-type alkyl.
-
- Iin which R1 C3-C5 non-branch type alkyl, and R2 is C6-C12 branch-type alkyl.
-
- The ester compound according to an embodiment of the present invention improves plasticization efficiency and the processability of a resin when used as a plasticizer, and provides good physical properties such as tensile strength, elongation rate, migration resistance, volatile loss, etc.
- Hereinafter, the present invention will be explained in detail to assist the understanding of the present invention.
- It will be understood that terms or words used in the present disclosure and claims should not be interpreted as having a meaning that is defined in common or in dictionaries, however should be interpreted in consistent with the technical scope of the present invention based on the principle that inventors may appropriately define the concept of the terms to explain the invention at his best method.
-
- That is, the ester composition includes an isophthalate-based ester compound in which ester groups (-COO-) are present at positions 1 and 3 in a benzene ring, that is, at a meta position, is more eco-friendly, has better physical properties including tensile strength, elongation rate, migration loss, volatile loss, etc., and has good processability and workability of a product when compared to a phthalate-based ester compound having ester groups (-COO-) at other positions, for example, an ortho position (positions 1 and 2 in a benzene ring) or a para position (positions 1 and 4 in a benzene ring).
- In contrast, a phthalate-based compound in which ester groups are present at an ortho position (positions 1 and 2 in a benzene ring) is an environmental hormone disturbing endocrine system and harmful to a human body, and have a limit in improving the processability of a resin, absorption rate with a resin, the degree of migration loss, and heat stability.
- In addition, terephthalate-based ester compound having ester groups at para position has relatively deteriorated compatibility and combination stability with the resin due to the linear structure thereof, and these defects may be adversely affecting factors to the processability and workability of a product.
- In the case of using the ester-based compound according to an embodiment of the present invention as the plasticizer of the resin composition, equivalent tensile strength and elongation rate may be secured when compared to a common phthalate-based compound widely used as a plasticizer. In addition, volatile loss may be decreased, and migration resistance may be markedly excellent.
- A compound in which R1 is a non-branch type, and R2 is a branch type may have improved hardness, tensile strength and elongation rate when compared to a compound in which both R1 and R2 have a branch type or a non-branch type. In addition, the productivity and processability of a final product may be improved due to the improved tensile strength and elongation rate.
- According to another embodiment of the present invention, in the above Formulae 1 to 3, R2 may be selected from ethylhexyl, isononyl, and propylheptyl.
-
-
-
-
-
- According to an embodiment of the present invention, the compounds of Formula 1, Formula 2 and Formula 3 may be included in an amount ratio of 0.5 to 50 wt%, 0.5 to 70 wt% and 0.5 to 85 wt% with respect to the total amount of the ester composition, respectively, and particularly, in an amount ratio of 0.5 to 50 wt%, 10 to 50 wt% and 35 to 80 wt%.
- According to an embodiment of the present invention, the mixing ratio of the total amount of the non-hybrid type compounds of Formulae 1 and 3 and the hybrid type compound of Formula 2 may be 95:5 to 30:70, and preferably, 90:10 to 60:40 by weight.
- According to an embodiment of the present invention, the ester-based composition includes the isophthalate-based compounds of Formulae 1 to 3 in the above-described specific amount range and so, is eco-friendly and has short absorption rate and short melting time with respect to a resin to improve the processability of the resin. In addition, physical properties such as hardness, tensile strength, elongation rate, migration loss, sheet volatile loss, heat stability, QUV, etc. may be further improved.
- The ester-based composition according to an embodiment of the present invention may be an ether-free plasticizer, and in this case, plasticizing efficiency is good, and workability is good.
- Ether-free composition means an ester-based composition in which an ether component included in the composition is 1,000 ppm and less, 100 ppm and less, or 10 ppm and less.
- According to an embodiment of the present invention, there is provided a preparation method of the ester-based composition including conducting a trans-esterification reaction of a compound of the following Formula 3 with a first alcohol of the following Formula 4.
<Formula 4> R1-OH
with R1 and R2 as defined in claim 1. -
- According to an embodiment of the present invention, by conducting the trans-esterification reaction, the compound of Formula 1 may be produced when the alkoxide of the first alcohol of Formula 4 attacks two carbon atoms of the ester group (RCOOR") of the compound of Formula 3, the compound of Formula 2 may be produced when the alkoxide attacks one carbon atom of the ester group (RCOOR") of the compound of Formula 3, and the compound of Formula 3 may remain as an unreacted part.
- In addition, the trans-esterification reaction may not induce defects concerning waste water when compared to an esterification reaction between acid-alcohol, and may not induce defects generated when using an acid catalyst because the trans-esterification reaction may be conducted without a catalyst.
- According to an embodiment of the present invention, through the trans-esterification reaction, the compound of Formula 1, the compound of Formula 2 and the compound of Formula 3 may be produced in an amount of 0.5 to 50 wt%, 0.5 to 70 wt% and 0.5 to 85 wt%, respectively, with respect to the total amount of the ester-based composition, and particularly in an amount of 0.5 to 50 wt%, 10 to 50 wt% and 35 to 80 wt%.
- In the above-described range, an ester-based composition having high process efficiency as a plasticizer and having good processability and absorption rate may be obtained.
- According to an embodiment of the present invention, the ester-based composition prepared by the trans-esterification reaction may include all of the compound of Formula 1, the compound of Formula 2 and the compound of Formula 3, and the composition of the ester-based composition may be controlled according to the amount added of the first alcohol of Formula 4.
- According to an embodiment of the present invention, the amount added of the first alcohol of Formula 4 may be 0.1 to 89.9 parts by weight, particularly, 3 to 50 parts by weight, and more particularly, 5 to 40 parts by weight with respect to 100 parts by weight of the compound of Formula 3.
- According to an embodiment of the present invention, as the amount added of the first alcohol of Formula 4 increases, the mole fraction of the compound of Formula 3 participating in the trans-esterification reaction may be increased, and the amount of the compound of Formula 1 and the compound of Formula 2 may be increased in the ester-based composition.
- In addition, the amount of the unreacted compound of Formula 3 may be decreased correspondingly.
- According to an embodiment of the present invention, the molar ratio of the compound of Formula 3 and the first alcohol of Formula 4 may be, for example, 1 : 0.005 to 5.0, 1 : 0.05 to 2.5, or 1 : 0.1 to 1.0, and in this range, an ester-based composition having high process efficiency and processability improving effects may be obtained.
- According to an embodiment of the present invention, the trans-esterification reaction may preferably be conducted under the reaction temperature of 120°C to 190°C, preferably 135°C to 180°C, and more preferably, 141°C to 179°C, for from 10 minutes to 10 hours, preferably from 30 minutes to 8 hours, and more preferably from 1 to 6 hours. Within the temperature range and the time period range, an ester-based composition having a desired composition may be effectively obtained. In this case, the reaction time may be calculated after elevating the temperature from the time of attainment of the reaction temperature.
- According to an embodiment of the present invention, the trans-esterification reaction may be conducted in the presence of an acid catalyst or a metal catalyst, and in this case, the reaction time may be decreased.
- The acid catalyst may be sulfuric acid, methanesulfonic acid, p-toluenesulfonic acid, etc., and the metal catalyst may be an organometallic catalyst, a metal oxide catalyst, a metal salt catalyst, a metal itself, etc.
- The metal component may be at least one selected from the group consisting of tin, titanium and zirconium, or a mixture of at least two thereof.
- In addition, according to an embodiment of the present invention, a removing process for removing the unreacted alcohol and reaction by-products, for example, the compound of Formula 3 by distillation may be further included after conducting the trans-esterification reaction.
- The distillation may be, for example, two-step distillation for separating the first alcohol of Formula 4 from the by-products using the difference between boiling points thereof.
- In another embodiment, the distillation may be mixed distillation. In this case, the ester-based composition may be relatively stably secured with desired composition. The mixed distillation means the distillation of butanol and the by-products at the same time.
- Meanwhile, the compound of Formula 3 used in the trans-esterification reaction of the present invention may be obtained by conducting an esterification reaction of the compound of the following Formula 5 with the second alcohol of the following Formula 6 or a mixture of the second alcohol with at least one isomer thereof in the presence of a catalyst.
<Formula 6> R2-OH
- In the above formulae, R2 is alkyl of C1-C20.
- The esterification reaction may be conducted under the reaction temperature of 80°C to 270°C, preferably 150°C to 250°C, for from 10 minutes to 10 hours, preferably from 30 minutes to 8 hours, and more preferably from 1 to 6 hours. Within the temperature range and the time period range, the compound of Formula 1 may be effectively obtained.
- According to an embodiment of the present invention, the catalyst used in the esterification reaction may be an organometallic catalyst including a Sn-based or a Ti-based catalyst, an acid catalyst including a sulfonic acid-based or a sulfuric-based catalyst, or a mixture catalyst thereof, and the kind of the catalyst is not limited.
- According to an embodiment of the present invention, the compound of Formula 5 and the second alcohol of Formula 6 (or a mixture of the second alcohol and at least one isomer thereof) may be used in a molar ratio of 1 : 1 to 7, and preferably, 1 : 2 to 5.
- According to an embodiment of the present invention, the second alcohol of the above Formula 6 may be used by preparing a common method or may be available on the market. When using the commercially available product, the second alcohol of the above Formula 6 may be included as a mixture with at least one isomer thereof, and the amount of the second alcohol of Formula 6 : the isomer thereof may be, for example, 50 to 100 parts by weight : 0 to 50 parts by weight, and preferably 70 to 100 parts by weight : 0 to 30 parts by weight.
-
- Particularly, the second alcohol of the above Formula 6 or the mixture of the second alcohol and the isomer thereof may be commercially available. For example, in the case of 2-propylheptane-1-ol, CAS No. 10042-59-8, 66256-62-0, 159848-27-8, etc. of BASF Co. including the isomer thereof may be purchased and used, and in the case of isononyl alcohol, CAS No. 68526-84-1 of EXXONMOBILE Co., CAS No. 27458-94-2 (68515-81-1) of KYOWA Co., etc. including the isomer thereof may be purchased and used. However, the present invention is not limited thereto.
- According to an embodiment of the present invention, in the case of using the second alcohol of Formula 6 including the isomer, a mixture of the compound of Formula 3 and the isomer thereof may be prepared. Thus, the ester-based composition according to an embodiment of the present invention may further include the compound of the above Formulae 1 to 3, preferably the compound of Formulae 2 and 3 may further include the isomer thereof, respectively.
- By the esterification reaction to prepare the compound of the above Formula 3 according to an embodiment of the present invention, the compound of Formula 3 may be prepared with the yield of about 80% and over. Through the trans-esterification reaction of the compound of Formula 3 thus prepared and the first alcohol of the above Formula 4, the ester-based composition having a desired composition may be easily prepared.
- Meanwhile, the present invention provides an ester-based composition prepared by the above preparation method.
- The ester-based composition according to an embodiment of the present invention has short absorption rate and short melting time with respect to the resin, and the processability of the resin may be improved, and good physical properties may be provided when prescribing a sheet and a compound such as a cable, an interior material of a vehicle, a film, a sheet, a tube, a wall paper, a toy, a flooring material, etc.
- Particularly, good physical properties may be obtained when prescribing the resin composition including the ester-based composition as a plasticizer as the wall paper sheet.
- Hereinafter, embodiments will be explained in detail to particularly explain the present invention. The present invention may, however, be embodied in different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of the inventive concept to those skilled in the art.
- To a four-necked, 3 liter reactor equipped with a cooler, a water stripper, a condenser, a decanter, a reflux pump, a temperature controller, a stirrer, etc., 498.4 g of purified isophthalic acid (PIA), 1,172.1 g of ethylhexyl alcohol (molar ratio of isophthalic acid : ethylhexyl alcohol was 1:3) and 1.54 g of tetraisopropyl titanate (TIPT) as a titanium-based catalyst (0.3 parts by weight on the basis of 100 parts by weight of isophthalic acid) were inserted, followed by slowly elevating the temperature to about 170°C. The generation of water began at about 170°C. An esterification reaction was conducted at the reaction temperature of about 220°C under an atmospheric pressure while continuously injecting a nitrogen gas for about 4.5 hours, and the reaction was terminated when an acid value reached 0.01.
- After completing the reaction, distillation-extraction under a reduced pressure was conducted for 0.5 to 4 hours to remove unreacted raw materials. To remove the unreacted raw materials to a certain amount degree and less, steam extraction was conducted using steam under a reduced pressure for 0.5 to 3 hours. The temperature of the reactant was lowered to about 90°C, and neutralization treatment was conducted using an alkaline solution. In addition, washing may be conducted, followed by dehydrating the reactant to remove water. A filter medium was inserted to the dehydrated reactant, followed by stirring for a certain time and filtering to finally obtain 1,162 g of di-(2-ethylhexyl) isophthalate (yield 99.0%).
- Bis-(2-propylheptyl) isophthalate was obtained by conducting the same procedure described in Preparation Example 1 except for using 2-propylheptyl alcohol (2-propylheptane-1-ol (85-100 %), 1-hexanol; 4-methyl-2-propyl (0-15%); 1-hexanol, 5-methyl-2-propyl (0-15%)) (CAS No. 10042-59-8, 66256-62-0 and 159848-27-8 of BASF Co.) instead of ethylhexyl alcohol.
- Bis(isononyl) isophthalate was obtained by conducting the same procedure described in Preparation Example 1 except for using isononyl alcohol (CAS No. 68526-84-1 of EXXONMOBILE Co.) instead of ethylhexyl alcohol.
- Bis(isodecyl) isophthalate was obtained by conducting the same procedure described in Preparation Example 1 except for using isodecyl alcohol instead of ethylhexyl alcohol.
- To a reactor equipped with a stirrer, a condenser and a decanter, 1,000 g of di-(2-ethylhexyl) isophthalate (hereinafter, DEHIP) prepared in Preparation Example 1 and 70 g of butanol (7 parts by weight on the basis of 100 parts by weight of DEHIP) were added, and a trans-esterification reaction was conducted under a nitrogen atmosphere at the reaction temperature of 140°C for 5 hours without a catalyst to produce an ester-based composition including 1.5 wt%, 22.4 wt% and 76.1 wt% of the compounds of the following Formula 1-1, Formula 2-1 and Formula 3-1, respectively.
- The reaction product was mixed distilled to remove butanol and 2-ethylhexyl alcohol and to finally prepare an ester-based composition.
- An ester-based composition including 1.4 wt%, 20.7 wt% and 77.9 wt% of the compounds of the following Formula 1-1, Formula 2-2 and Formula 3-2, respectively, was obtained by conducting the same procedure described in Example 1 except for using bis(2-propylheptyl) isophthalate obtained in Preparation Example 2 instead of di-(2-ethylhexyl) isophthalate (hereinafter, DEHIP) obtained in Preparation Example 1.
- An ester-based composition including 1.5 wt%, 21.3 wt% and 77.2 wt% of the compounds of the following Formula 1-1, Formula 2-3 and Formula 3-3, respectively, was obtained by conducting the same procedure described in Example 1 except for using bis(isononyl) isophthalate obtained in Preparation Example 2 instead of di-(2-ethylhexyl) isophthalate (hereinafter, DEHIP) obtained in Preparation Example 1.
- An ester-based composition including 1.4 wt%, 20.5 wt% and 78.1 wt% of the compounds of the following Formula 1-1, Formula 2-4 and Formula 3-4, respectively, was obtained by conducting the same procedure described in Example 1 except for using bis(isodecyl) isophthalate obtained in Preparation Example 4 instead of di-(2-ethylhexyl) isophthalate (hereinafter, DEHIP) obtained in Preparation Example 1.
- Ester-based compositions having the composition of the compounds of Formula 1, Formula 2 and Formula 3 were obtained by conducting the same procedure described in Example 1 except for controlling the amount of the butanol as described in the following Table 1.
- To a four-necked, 3 liter reactor equipped with a cooler, a water stripper, a condenser, a decanter, a reflux pump, a temperature controller, a stirrer, etc., 498.4 g of purified isophthalic acid, 1,015.8 g of ethylhexyl alcohol, 1,067 g of 2-propyheptanol and 15 g of methanesulfonic acid (MSA) as a catalyst (3 parts by weight on the basis of 100 parts by weight of PTA) were inserted, followed by slowly elevating the temperature to about 210°C. The generation of water began at about 170°C. An esterification reaction was conducted at the reaction temperature of about 210°C under an atmospheric pressure while continuously injecting a nitrogen gas for about 4 hours, and the reaction was terminated when an acid value reached 4.
- After completing the reaction, distillation-extraction under a reduced pressure was conducted for 0.5 to 4 hours to remove unreacted raw materials. To remove the unreacted raw materials to a certain amount degree and less, steam extraction was conducted using steam under a reduced pressure for 0.5 to 3 hours. The temperature of the reactant was lowered to about 90°C, and neutralization treatment was conducted using an alkaline solution. In addition, washing may be conducted, followed by dehydrating the reactant to remove water. A filter medium was inserted to the dehydrated reactant, followed by stirring for a certain time and filtering to finally obtain 2 wt% of DEHIP, 25 wt% of 2-propylheptyl ethylhexyl isophthalate (PHEHIP) and 73 wt% of bis(2-propylheptyl) isophthalate (DPHIP).
- A reaction product including 75.5 wt% of di-(2-ethylhexyl) terephthalate (DEHTP), 22.8 wt% of 1-butyl 4-(2-ethylhexyl) terephthalate (hereinafter, BEHTP) and 1.7 wt% of dibutyl terephthalate (hereinafter, DBTP) was obtained by conducting the same procedure described in Preparation Example 1 and Example 1 using terephthalic acid instead of isophthalic acid prepared in Preparation Example 1.
- A reaction product including 75.0 wt% of di-(2-ethylhexyl) terephthalate (DEHP), 22.5 wt% of 1-butyl 4-(2-ethylhexyl) terephthalate (hereinafter, BEHP) and 2.5 wt% of dibutyl phthalate (hereinafter, DBP) was obtained by conducting the same procedure described in Preparation Example 1 and Example 1 using phthalic acid instead of isophthalic acid prepared in Preparation Example 1.
[Table 1] Butanol amount (parts by weight) Formula 1 (wt%) Formula 2 (wt%) Formula 3 (wt%) Example 1 (1P) 7 parts by weight (Formula 1-1) 1.5 (Formula 2-1) 22.4 (Formula 3-1) 76.1 Example 2 (1P) 7 parts by weight (Formula 1-1) 1.4 (Formula 2-2) 20.7 (Formula 3-2) 77.9 Example 3 (1P) 7 parts by weight (Formula 1-1) 1.5 (Formula 2-3) 21.3 (Formula 3-3) 77.2 Example 4 (1P) 7 parts by weight (Formula 1-1) 1.4 (Formula 2-4) 20.5 (Formula 3-4) 78.1 Example 5 (1P) 4 parts by weight (Formula 1-1) 0.6 (Formula 2-1) 14.4 (Formula 3-1) 85.0 Example 6 (1P) 10 parts by weight (Formula 1-1) 2.8 (Formula 2-1) 28.4 (Formula 3-1) 68.8 Example 7 (1P) 13 parts by weight (Formula 1-1) 3.1 (Formula 2-1) 29.8 (Formula 3-1) 67.1 Example 8 (1P) 15 parts by weight (Formula 1-1) 4.8 (Formula 2-1) 35.1 (Formula 3-1) 60.1 Example 9 (1P) 18 parts by weight (Formula 1-1) 6.9 (Formula 2-1) 39.4 (Formula 3-1) 53.7 Example 10 (1P) 20 parts by weight (Formula 1-1) 7.9 (Formula 2-1) 41.1 (Formula 3-1) 51.0 Example 11 (1P) 22 parts by weight (Formula 1-1) 9.0 (Formula 2-1) 42.7 (Formula 3-1) 48.3 Example 12 (1P) 30 parts by weight (Formula 1-1) 12.5 (Formula 2-1) 46.3 (Formula 3-1) 41.2 Example 13 (1P) 40 parts by weight (Formula 1-1) 17.9 (Formula 2-1) 49.4 (Formula 3-1) 41.7 Comparative Example 1 (1P) 7 parts by weight (DEHTP) 2.0 (PHEHIP) 25.0 (DPHIP) 73.0 Comparative Example 2 (TP) 7 parts by weight (DBTP) 1.7 (BEHTP) 22.8 (DEHTP) 75.5 Comparative Example 3 (1P) 7 parts by weight (DBP) 2.5 (BEHP) 22.5 (DEHP) 75.0 - In the ester-based compositions of Examples 1 to 13 of the present invention and Comparative Examples 1 to 3, the amount (wt%) of each compound was measured using a gas chromatography apparatus of Agilent Co. (Agilent 7890 GC, Column: HP-5, carrier gas: helium).
- In the ester-based compositions of Examples 1 to 13, ether was not detected.
- For the ester-based compositions prepared in Examples 1 to 13 and Comparative Examples 1 to 3, 55 parts by weight of a plasticizer, 2 parts by weight of a BZ stabilizer (BZ210, Songwon Industries) as an additive and 2 parts by weight of an epoxidized soybean oil (ESO, Songwon Industries) with respect to 100 parts by weight of a polyvinyl chloride resin (PVC, LS 130s) were mixed in a rotational rate of 1,300 rpm at 100°C. A process was conducted using a roll mill at 175 for 4 minutes and using a press at 185°C for 3 minutes (low pressure) and for 2 minutes and 30 seconds (high pressure) to manufacture a sheet to a thickness of 2 mm.
- With respect to the sheet, hardness, tensile strength, elongation rate, migration loss and sheet volatile loss was measured.
- The evaluation conditions of each performance were as follows.
- Shore hardness (Shore A) at 25°C was measured using ASTM D2240.
-
-
- According to KSM-3156, a specimen with a thickness of 2 mm and over was obtained, ABS (natural color) was attached onto both sides of the specimen and a load of 1 kgf/cm2 was applied. The specimen was stood in a hot air circulation type oven (80°C) for 72 hours and then taken out and cooled at room temperature for 4 hours. Then, the ABS attached onto both sides of the specimen was removed, the weights before and after standing in the oven were measured, and the migration loss was calculated by the following equation.
- The specimen thus manufactured was processed at 70°C for 72 hours, and the weight of the specimen was measured.
[Table 2] Example/Comparative Example Example 1 Example 2 Example 3 Example 4 Comparative Example 1 R1 and R2 R1: butyl R2: ethylhexyl R1: butyl R2: propylheptyl R1: butyl R2: isononyl R1: butyl R2: isodecyl R1: ethylhexyl R2: propylheptyl Reaction Trans-esterification Trans-esterification Trans-esterification Trans-esterification Esterification reaction Physical properties Hardness (Shore A) 87.0 90.5 88.5 90.8 91.8 Tensile strength (kg/cm2) 223.2 231.2 225.7 230.1 232.9 Elongation rate (%) 306.5 287.3 290.6 288.5 278.0 - The results of the above Table 2 are obtained by measuring the physical properties using the ester-based compositions of Examples 1 to 4 and Comparative Example 1 according to the trans-esterification reaction or esterification reaction, and branch/non-branch type of R1 and R2.
- As shown in the above Table 2, the ester-based compositions of Examples 1 to 4 of the present invention prepared by the trans-esterification reaction have markedly improved hardness, tensile strength and elongation rate when compared to those of the ester-based composition of Comparative Example 1.
- When particularly examining, the ester-based compositions of Examples 1 to 4 of the present invention, particularly, the ester-based compositions of Examples 1 to 4 in which R1 is a non-branch type, and R2 is a branch type by the trans-esterification reaction have better hardness, tensile strength and elongation rate when compared to the ester-based composition of Comparative Example 1 in which both R1 and R2 have a branch type.
- For example, the hardness of the ester-based compositions of Examples 1 to 4 is decreased by 5% and over when compared to the ester-based composition of Comparative Example 1. Since the hardness is decreased as in the examples of the present invention, good processability and the stabilization of workability may be provided when applied in a practical product.
- In addition, it would be known that the elongation rate is increased by about 4% and over for the ester-based compositions of Examples 1 to 4 when compared to that of the ester-based composition of Comparative Example 1.
[Table 3] Butanol amount Hardness (Shore A) Tensile strength (kg/cm2) Elongation rate (%) Migration loss (%) Example 5 4 parts by weight 87.5 230.5 309.5 0.08 Example 6 10 parts by weight 87.0 220.3 305.6 0.11 Example 7 13 parts by weight 86.7 220.1 306.7 0.13 Example 8 15 parts by weight 86.5 219.5 304.5 0.13 Example 9 18 parts by weight 86.4 219.1 307.5 0.14 Example 10 20 parts by weight 86.2 219.2 305.3 0.16 Example 11 22 parts by weight 85.8 219.0 296.5 0.30 Example 12 30 parts83.5 by weight 85.0 205.3 285.1 0.60 Example 13 40 parts by weight 83.5 197.6 272.3 1.23 - The above Table 3 shows the hardness, tensile strength, elongation rate and migration resistance of the ester-based compositions of Examples 5 to 13 according to the amount added of butanol.
- As shown in the above Table 3, the hardness, tensile strength, elongation rate and migration resistance are markedly changed according to the amount added of butanol.
- Particularly, the hardness, tensile strength and elongation rate are relatively improved while the migration resistance is decreased according to the decrease of the amount added of butanol.
- Accordingly, the physical properties may be controlled according to use by controlling the amount of butanol, and it would be secured that the ester-based compositions may be usefully applied.
[Table 4] Example/Comparative example Example 1 Comparative Example 2 Comparative Example 3 Acid Isophthalic acid Terephthalic acid Phthalic acid Reaction Trans-esterification Trans-esterification Trans-esterification Physical properties Hardness (Shore A) 87.0 87.7 87.3 Tensile strength (kg/cm2) 223.2 232.1 221.6 Elongation rate (%) 306.5 278.5 304.8 Migration loss (%) 0.10 0.08 1.23 Volatile loss (%) 6.20 7.52 8.96 - Table 4 shows the results of the hardness, tensile strength, elongation rate and migration resistance of the sheets manufactured using the plasticizers of Example 1 and Comparative Examples 2 and 3 by changing the kinds of an acid.
- As shown in the above Table 4, the elongation rate is improved, and the effects of migration resistance and volatile loss are good for the ester-based compositions of the examples of the present invention using an isophthalate-based ester plasticizers when compared to the ester-based compositions of Comparative Examples 2 and 3 using terephthalate-based and phthalate-based ester plasticizers.
- Particularly, for the specimen using the isophthalate-based ester plasticizer of the present invention, the elongation rate, migration resistance and volatile loss are improved when compared to the phthalate-based and terephthalate-based ester plasticizer having ester groups at ortho position and para position. Thus, the processability of a resin, absorption rate with the resin, the degree of migration loss and heat stability are improved.
- Particularly, the migration resistance of the specimen of Example 1 of the present invention may be decreased 10 times and less when compared to that of Comparative Example 3.
- In addition, the volatile loss of the specimen of Example 1 of the present invention may decrease to about 20 to 45% when compared to that of Comparative Examples 2 and 3.
- The decrease of the volatile loss as in Comparative Examples 2 and 3 may be a fatal defect in the processability and the stability for a long time of a final product. That is, the increase of the volatile loss means the decrease of the amount of the ester-based composition (plasticizer) present in the specimen and the deterioration of the elongation rate.
- Thus, it would be secured that the physical properties of the isophthalate-based ester plasticizer of the present invention are markedly increased when compared to a terephthalate-based and phthalate-based plasticizers.
- To a four-necked, 3 liter reactor equipped with a cooler, a water stripper, a condenser, a decanter, a reflux pump, a temperature controller, a stirrer, etc., 498.4 g of purified isophthalic acid (PIA), 1,425 g of 2-propylheptanol (2-PH) (BASF Co., including 80-100 wt% of 2-PH, 0-15 wt% of 4-methyl-2-propyl hexanol and 0-15 wt% of 5-methyl-2-propyl-hexanol) (molar ratio of isophthalic acid : 2-PH was 1:3) and 1.54 g of tetra isopropyl titanate (TIPT) as a titanium-based catalyst were inserted, followed by slowly elevating the temperature to about 170°C. The generation of water began at about 170°C. An esterification reaction was conducted at the reaction temperature of about 220°C under an atmospheric pressure while continuously injecting a nitrogen gas for about 4.5 hours, and the reaction was terminated when an acid value reached 0.01.
- After completing the reaction, distillation-extraction under a reduced pressure was conducted for 0.5 to 4 hours to remove unreacted raw materials. The reactant was cooled, and neutralization treatment was conducted using an alkaline solution. In addition, the reactant was dehydrated to remove water. A filter medium was inserted to the dehydrated reactant, followed by stirring for a certain time and filtering to finally obtain 1,162 g of di-(2-propylheptyl) isophthalate (yield 99.0%).
- To a reactor equipped with a stirrer, a condenser and a decanter, 1,000 g of di-(2-propylheptyl) isophthalate (hereinafter, DPHIP) prepared in Preparation Example 5 and 70 g of butanol (7 parts by weight on the basis of 100 parts by weight of DPHIP) were added, and a trans-esterification reaction was conducted under a nitrogen atmosphere at the reaction temperature of 140°C for 5 hours without a catalyst to produce an ester-based composition including 21.0 wt%, 1.6 wt% and 77.4 wt% of the compounds of the following Formula 2-2, Formula 1-1 and Formula 3-2, respectively.
- Ester-based compositions having the compositions of Formula 2-2, Formula 1-1 and Formula 3-2 in the following Table 5 were obtained by conducting the same procedure described in Example 14 except for controlling the amount of butanol as described in the following Table 5.
- A reaction product including 75.4 wt% of di-(2-propylheptyl) terephthalate (DPHTP), 23.2 wt% of 1-butyl 4-(2-propylheptyl) terephthalate (hereinafter, BPHTP) and 1.4 wt% of dibutyl terephthalate (hereinafter, DBTP) was obtained by conducting the same procedure described in Preparation Example 2 and Example 14 using terephthalic acid instead of isophthalic acid prepared in Preparation Example 2.
- A reaction product including 74.5 wt% of di-(2-propylheptyl) phthalate (DPHP), 22.1 wt% of 1-butyl 4-(2-propylheptyl) phthalate (hereinafter, BPHP) and 3.4 wt% of dibutyl phthalate (hereinafter, DBP) was obtained by conducting the same procedure described in Preparation Example 2 and an example using phthalic acid instead of isophthalic acid prepared in Preparation Example 2.
[Table 5] Butanol amount (parts by weight) Formula 1-1 (wt%) Formula 2-2 (wt%) Formula 3-2 (wt%) Example 14 (1P) 7 parts by weight Formula 1-1 1.6 Formula 2-2 21.0 Formula 3-2 77.4 Example 15 (1P) 4 parts by weight Formula 1-1 0.6 Formula 2-2 14.7 Formula 3-2 84.7 Example 16 (1P) 10 parts by weight Formula 1-1 2.6 Formula 2-2 28.5 Formula 3-2 68.9 Example 17 (1P) 15 parts by weight Formula 1-1 5.2 Formula 2-2 36.1 Formula 3-2 58.7 Example 18 (1P) 20 parts by weight Formula 1-1 8.0 Formula 2-2 41.3 Formula 3-2 50.7 Example 19 (1P) 22 parts by weight Formula 1-1 9.2 Formula 2-2 43.0 Formula 3-2 47.8 Example 20 (1P) 30 parts by weight Formula 1-1 12.8 Formula 2-2 46.5 Formula 3-2 40.7 Example 21 (1P) 40 parts by weight Formula 1-1 18.5 Formula 2-2 49.8 Formula 3-2 31.7 Comparative Example 4 (TP) 7 parts by weight (DBTP) 1.4 (BPHTP) 23.2 (BPHTP) 75.4 Comparative Example 5 (P) 7 parts by weight (DBP) 3.4 (BPHP) 22.1 (DPHP) 74.5 - In the ester-based compositions of Examples 14 to 21 of the present invention and Comparative Examples 4 to 5, the amount (wt%) of each compound was measured using a gas chromatography apparatus of Agilent Co. (Agilent 7890 GC, column: HP-5, carrier gas: helium).
- In the ester-based compositions of Examples 14 to 21, ether was not detected.
- For the ester-based composition prepared in Examples 14 to 21 and Comparative Examples 3 to 5, 55 parts by weight of a plasticizer, 2 parts by weight of a BZ stabilizer (BZ210, Songwon Industries) as an additive and 2 parts by weight of an epoxidized soybean oil (ESO, Songwon Industries) with respect to 100 parts by weight of a polyvinyl chloride resin
- (PVC, LS 130s) were mixed in a rotational rate of 1,300 rpm at 100°C. A process was conducted using a roll mill at 175°C for 4 minutes and using a press at 185°C for 3 minutes (low pressure) and for 2 minutes and 30 seconds (high pressure) to manufacture a sheet with a thickness of 2 mm.
- With respect to the sheet, hardness, tensile strength, elongation rate, migration loss and sheet volatile loss were measured. The results are illustrated in Tables 6 and 7.
[Table 6] Butanol amount Hardness (Shore A) Tensile strength (kg/cm2) Elongation rate (%) Migration loss (%) Example 15 4 parts by weight 92.6 268.7 256.3 0.02 Example 16 10 parts by weight 91.2 249.5 267.5 0.03 Example 17 15 parts by weight 90.3 235.1 280.5 0.03 Example 18 20 parts by weight 88.7 218.6 296.8 0.05 Example 19 25 parts by weight 86.9 213.2 316.4 0.07 Example 20 30 parts by weight 85.8 205.6 320.6 0.10 Example 21 40 parts by weight 85.0 198.3 332.3 0.18 - The above Table 6 shows the hardness, tensile strength, elongation rate and migration resistance of the ester-based compositions of Examples 15 to 21 according to the amount added of butanol.
- As shown in the above Table 6, the hardness, tensile strength, elongation rate and migration resistance are markedly changed according to the amount added of butanol.
- Particularly, the hardness, tensile strength and elongation rate are relatively improved while the migration resistance is decreased according to the decrease of the amount added of butanol.
- Accordingly, the physical properties may be controlled according to use by controlling the amount of butanol, and it would be secured that the ester-based compositions may be usefully applied.
[Table 7] Example/Comparative example Example 14 Comparative Example 4 Comparative Example 5 Acid Isophthalic acid Terephthalic acid Phthalic acid Reaction Trans-esterification Trans-esterification Trans-esterification Physical properties Hardness (Shore A) 91.8 93.5 92.0 Tensile strength (kg/cm2) 256.5 284.3 257.8 Elongation rate (%) 260.4 235.1 255.8 Migration loss (%) 0.03 0.07 0.03 Volatile loss (%) 0.67 1.11 0.87 - Table 7 shows the results of the hardness, tensile strength, elongation rate and migration resistance of the sheets manufactured using the plasticizers of Example 14 and Comparative Examples 4 and 5 by changing the kinds of an acid.
- As shown in the above Table 7, the elongation rate is improved, and the effects of migration resistance and volatile loss are good for the ester-based compositions of the examples of the present invention using an isophthalate-based ester plasticizers when compared to the ester-based compositions of Comparative Examples 4 and 5 using terephthalate-based and phthalate-based ester plasticizers.
- Particularly, for the specimen using the isophthalate-based ester plasticizer of the present invention, the elongation rate, migration resistance and volatile loss are improved when compared to the phthalate-based and terephthalate-based ester plasticizer having ester groups at ortho position and para position. Thus, the processability of a resin, absorption rate with the resin, the degree of migration loss and heat stability are improved.
- In addition, the volatile loss of the specimen of Example 14 of the present invention may decrease to about 30 to 65% when compared to that of Comparative Examples 4 and 5.
- The increase of the volatile loss as in Comparative Examples 4 and 5 may be a fatal defect in the processability and the stability for a long time of a final product. That is, the increase of the volatile loss means the decrease of the amount of the ester-based composition (plasticizer) present in the specimen and the deterioration of the elongation rate.
- Thus, it may be secured that the physical properties of the isophthalate-based ester plasticizer of the present invention be markedly increased when compared to those of a terephthalate-based and phthalate-based plasticizers.
- To a four-necked, 3 liter reactor equipped with a cooler, a water stripper, a condenser, a decanter, a reflux pump, a temperature controller, a stirrer, etc., 498.4 g of purified isophthalic acid (PIA), 1,298.3 g of isononyl alcohol (CAS No. 68526-84-1 of EXXONMOBILE Co.) (molar ratio of isophthalic acid : isononyl alcohol was 1:3) and 1.54 g of tetra isopropyl titanate (TIPT) as a titanium-based catalyst were inserted, followed by slowly elevating the temperature to about 170°C. The generation of water began at about 170°C. An esterification reaction was conducted at the reaction temperature of about 220°C under an atmospheric pressure while continuously injecting a nitrogen gas for about 4.5 hours, and the reaction was terminated when an acid value reached 0.01.
- After completing the reaction, distillation-extraction under a reduced pressure was conducted for 0.5 to 4 hours to remove unreacted raw materials. The reactant was cooled, and neutralization treatment was conducted using an alkaline solution. In addition, the reactant was dehydrated to remove water. A filter medium was inserted to the dehydrated reactant, followed by stirring for a certain time and filtering to finally obtain 1,243.3 g of di-isononyl isophthalate (yield 99.0%).
- To a reactor equipped with a stirrer, a condenser and a decanter, 1,000 g of di-isononyl isophthalate (hereinafter, DINIP) prepared in Preparation Example 6 and 70 g of butanol (7 parts by weight on the basis of 100 parts by weight of DINIP) were added, and a trans-esterification reaction was conducted under a nitrogen atmosphere at the reaction temperature of 140°C for 5 hours without a catalyst to produce an ester-based composition including 21.3 wt%, 2.3 wt% and 77.2 wt% of the compounds of the following Formula 2-3, Formula 1-1 and Formula 3-3, respectively.
- The above reaction products were mixed distillated to remove butanol and isononyl alcohol to finally prepare an ester-based composition.
- Ester-based compositions having the compositions of Formula 2-3, Formula 1-1 and Formula 3-3 in the following Table 8 were obtained by conducting the same procedure described in Example 22 except for controlling the amount of butanol as described in the following Table 8.
- A reaction product including 75.1 wt% of di-(isononyl) terephthalate (DINTP), 23.0 wt% of 1-butyl 4-(isononyl) terephthalate (hereinafter, BINTP) and 1.9 wt% of dibutyl terephthalate (hereinafter, DBTP) was obtained by conducting the same procedure described in Preparation Example 3 and Example 22 using terephthalic acid instead of isophthalic acid prepared in Preparation Example 3.
- A reaction product including 75.9 wt% of di-(isononyl) phthalate (DNIP), 22.0 wt% of 1-butyl 4-(isononyl) phthalate (hereinafter, BINP) and 2.1 wt% of dibutyl phthalate (hereinafter, DBP) was obtained by conducting the same procedure described in Preparation Example 3 and Example 22 using phthalic acid instead of isophthalic acid prepared in Preparation Example 3.
[Table 8] Butanol amount (parts by weight) Formula 1-1 (wt%) Formula 2-3 (wt%) Formula 3-3 (wt%) Example 22 (1P) 7 parts by weight Formula 1-1 (2.3) Formula 2-3 (20.5) Formula 3-3 (77.2) Example 23 (1P) 4 parts by weight Formula 1-1 (0.7) Formula 2-3 (14.9) Formula 3-3 (84.4) Example 24 (1P) 10 parts by weight Formula 1-1 (2.9) Formula 2-3 (28.9) Formula 3-3 (68.2) Example 25 (1P) 15 parts by weight Formula 1-1 (5.0) Formula 2-3 (35.3) Formula 3-3 (59.7) Example 26 (1P) 20 parts by weight Formula 1-1 (7.9) Formula 2-3 (41.3) Formula 3-3 (51.8) Example 27 (1P) 25 parts by weight Formula 1-1 (10.5) Formula 2-3 (43.8) Formula 3-3 (45.7) Example 28 (1P) 30 parts by weight Formula 1-1 (12.2) Formula 2-3 (45.8) Formula 3-3 (42.0) Example 29 (1P) 40 parts by weight Formula 1-1 (18.0) Formula 2-3 (49.8) Formula 3-3 (32.2) Comparative Example 6 (TP) 7 parts by weight (DBTP) (1.9) (BINTP) (23.0) (DINTP) (75.1) Comparative Example 7 (P) 7 parts by weight (DBP) (2.1) (BINP) (22.0) (DINP) (75.9 - In the ester-based compositions of Examples 22 to 29 of the present invention and Comparative Examples 6 to 7, the amount (wt%) of each compound was measured using a gas chromatography apparatus of Agilent Co. (Agilent 7890 GC, column: HP-5, carrier gas: helium).
- In the ester-based compositions of Examples 22 to 29, ether was not detected.
- For the ester-based composition prepared in Examples 22 to 29 and Comparative Examples 6 to 7, 55 parts by weight of a plasticizer, 2 parts by weight of a BZ stabilizer (BZ210, Songwon Industries) as an additive and 2 parts by weight of an epoxidized soybean oil (ESO, Songwon Industries) with respect to 100 parts by weight of a polyvinyl chloride resin (PVC, LS 130s) were mixed in a rotational rate of 1,300 rpm at 100°C. A process was conducted using a roll mill at 175°C for 4 minutes and using a press at 185°C for 3 minutes (low pressure) and for 2 minutes and 30 seconds (high pressure) to manufacture a sheet with a thickness of 2 mm.
- With respect to the sheet, hardness, tensile strength, elongation rate, migration loss and sheet volatile loss were measured. The results are illustrated in Tables 9 and 10.
[Table 9] Butanol amount Hardness (Shore A) Tensile strength (kg/cm2) Elongation rate (%) Migration loss (%) Example 23 4 parts by weight 90.3 237.5 291.6 0.05 Example 24 10 parts by weight 88.5 224.6 303.4 0.06 Example 25 15 parts by weight 88.2 220.7 310.2 0.10 Example 26 20 parts by weight 87.6 216.8 316.5 0.14 Example 27 25 parts by weight 86.8 209.5 321.7 0.16 Example 28 30 parts by weight 85.9 201.3 330.1 0.17 Example 29 40 parts by weight 84.5 195.6 345.6 0.20 - The above Table 9 shows the hardness, tensile strength, elongation rate and migration resistance of the ester-based compositions of Examples 23 to 29 according to the amount added of butanol.
- As shown in the above Table 9, the hardness, tensile strength, elongation rate and migration resistance are markedly changed according to the amount added of butanol.
- Particularly, the hardness, tensile strength and elongation rate are relatively improved while the migration resistance is decreased according to the decrease of the amount added of butanol.
- Accordingly, the physical properties may be controlled according to use by controlling the amount of butanol, and it may be secured that the ester-based compositions may be usefully applied.
[Table 10] Example/Comparative example Example 22 Comparative Example 6 Comparative Example 7 Acid Isophthalic acid Terephthalic acid Phthalic acid Reaction Trans-esterification Trans-esterification Trans-esterification Physical properties Hardness (Shore A) 88.5 89.5 88.3 Tensile strength (kg/cm2) 225.7 254.6 220.9 Elongation rate (%) 290.6 240.8 284.3 Migration loss (%) 0.05 0.09 0.04 Volatile loss (%) 1.02 1.45 1.23 - Table 10 shows the results of the hardness, tensile strength, elongation rate and migration resistance of the sheets manufactured using the plasticizers of Example 22 and Comparative Examples 6 and 7 by changing the kinds of an acid.
- As shown in the above Table 10, the elongation rate is improved, and the effects of migration resistance and volatile loss are good for the ester-based composition of the example of the present invention using an isophthalate-based ester plasticizer when compared to the ester-based compositions of Comparative Examples 6 and 7 using terephthalate-based and phthalate-based ester plasticizers.
- Particularly, for the specimen using the isophthalate-based ester plasticizer of the present invention, the elongation rate, migration resistance and volatile loss are improved when compared to the phthalate-based and terephthalate-based ester plasticizer having ester groups at ortho position and para position. Thus, the processability of a resin, absorption rate with the resin, the degree of migration loss and heat stability are improved.
- In addition, the volatile loss of the specimen of Example 22 of the present invention may decrease to about 20 to 45% when compared to that of Comparative Examples 6 and 7.
- The increase of the volatile loss as in Comparative Examples 6 and 7 may be a fatal defect in the processability and the stability for a long time of a final product. That is, the increase of the volatile loss means the decrease of the amount of the ester-based composition (plasticizer) present in the specimen and the deterioration of the elongation rate.
- Thus, it may be secured that the physical properties of the isophthalate-based ester plasticizer composition of the present invention may be markedly increased when compared to a terephthalate-based and phthalate-based plasticizers.
Claims (20)
- The ester-based composition of claim 1, wherein R2 is selected from ethylhexyl, isononyl and propylheptyl.
- The ester-based composition of claim 1, wherein the compounds of Formula 1, Formula 2 and Formula 3 are comprised in amounts of 0.5 to 50 wt%, 0.5 to 70 wt% and 0.5 to 85 wt% with respect to a total amount of the ester-based composition.
- The ester-based composition of claim 3, wherein the compounds of Formula 1, Formula 2 and Formula 3 are comprised in amounts of 0.5 to 50 wt%, 10 to 50 wt% and 35 to 80 wt% with respect to a total amount of the ester-based composition.
- The ester-based composition of claim 3, wherein a ratio of a total amount of the compounds of Formulae 1 and 3 and an amount of the compound of Formula 2 is 95 : 5 to 30 : 70 by weight.
- The ester-based composition of claim 1, wherein the ester-based composition is an ether-free plasticizer,
wherein the ether-free plasticizer is the plasticizer in which an ether component included in the composition is 1,000 ppm and less. - A method of preparing the ester-based composition of claim 1 comprising conducting a trans-esterification reaction of a compound of the following Formula 3 with a first alcohol of the following Formula 4:
<Formula 4> R1-OH
in the above formulae, R1 is C3-C5 non-branch type alkyl, and R2 is C6-C12 branch-type alkyl. - The method of the ester-based composition of claim 12, wherein a molar ratio of the compound of the above Formula 3 and a first alcohol of the above Formula 4 is 1 : 0.005 to 5.
- The method of the ester-based composition of claim 12, wherein an amount of the first alcohol of the above Formula 4 is 0.1 to 89.9 parts by weight with respect to 100 parts by weight of the compound of the above Formula 3.
- The method of the ester-based composition of claim 12, wherein the trans-esterification reaction is a non-catalytic reaction.
- The method of the ester-based composition of claim 12, further comprising distilling unreacted first alcohol of Formula 4 and by-products to remove after the trans-esterification reaction.
- The method of the ester-based composition of claim 12, wherein a portion of the compound of the above Formula 3 is transformed into a compound of the following Formula 1 and a compound of the following Formula 2:
- The method of the ester-based composition of claim 12, wherein the compound of the above Formula 3 is obtained by an esterification reaction of a compound of the following Formula 5 and a second alcohol of the following Formula 6 in the presence of a catalyst:
<Formula 6> R2-OH
in the above formula, R2 is C1-C20 alkyl. - The method of the ester-based composition of claim 18, wherein the compound of the above Formula 5 and the second alcohol of the above Formula 6 are used in a molar ratio of 1 : 1 to 7.
- The method of the ester-based composition of claim 18, wherein the second alcohol of the above Formula 6 further comprises at least one isomer of the second alcohol.
Applications Claiming Priority (10)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR20140014203 | 2014-02-07 | ||
KR20140021409 | 2014-02-24 | ||
KR1020140154390A KR20150093580A (en) | 2014-02-07 | 2014-11-07 | Ester-based plasticizer, preparation method thereof, and resin composition comprising the same |
KR1020150017584A KR101705431B1 (en) | 2014-02-07 | 2015-02-04 | Ester-based compound, composition comprising the same, preparation method the composition, and resin composition comprising the composition |
KR1020150017583A KR101705430B1 (en) | 2014-02-07 | 2015-02-04 | Ester-based compound, composition comprising the same, preparation method the composition, and resin composition comprising the composition |
KR1020150017581A KR101841813B1 (en) | 2014-02-07 | 2015-02-04 | Ester-based plasticizer, preparation method thereof, and resin composition comprising the same |
KR1020150017582A KR101705429B1 (en) | 2014-02-07 | 2015-02-04 | Ester-based compound, composition comprising the same, preparation method the composition, and resin composition comprising the composition |
KR1020150017574A KR101720852B1 (en) | 2014-02-07 | 2015-02-04 | Isophthalate-based ester compound and plasticizer composition comprising the same |
KR1020150017573A KR101712718B1 (en) | 2014-02-07 | 2015-02-04 | Isophthalate-based esther compound, preparation method thereof, and resin composition comprising the same |
PCT/KR2015/001203 WO2015119443A1 (en) | 2014-02-07 | 2015-02-05 | Ester compound, plasticizer composition comprising same, method for manufacturing ester composition, and resin composition comprising ester composition |
Publications (3)
Publication Number | Publication Date |
---|---|
EP3103834A1 EP3103834A1 (en) | 2016-12-14 |
EP3103834A4 EP3103834A4 (en) | 2017-01-18 |
EP3103834B1 true EP3103834B1 (en) | 2019-04-03 |
Family
ID=53791920
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP14814674.9A Active EP2927210B1 (en) | 2014-02-07 | 2014-10-22 | Plasticizers, resin composition, and method for manufacturing plasticizers and resin composition |
EP15746898.4A Active EP3103834B1 (en) | 2014-02-07 | 2015-02-05 | Ester composition and method for its manufacturing |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP14814674.9A Active EP2927210B1 (en) | 2014-02-07 | 2014-10-22 | Plasticizers, resin composition, and method for manufacturing plasticizers and resin composition |
Country Status (9)
Country | Link |
---|---|
US (2) | US9714211B2 (en) |
EP (2) | EP2927210B1 (en) |
JP (1) | JP6402868B2 (en) |
KR (7) | KR101535392B1 (en) |
CN (3) | CN110734579A (en) |
ES (1) | ES2837976T3 (en) |
RU (1) | RU2670621C2 (en) |
TW (2) | TWI643844B (en) |
WO (1) | WO2015119355A1 (en) |
Families Citing this family (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWI643844B (en) * | 2014-02-07 | 2018-12-11 | Lg化學股份有限公司 | Plasticizer and resin composition, and preparation method thereof |
KR101784099B1 (en) | 2015-04-06 | 2017-10-10 | 주식회사 엘지화학 | Plasticizer, resin composition and method for preparing them |
KR101939160B1 (en) * | 2015-05-14 | 2019-01-16 | 주식회사 엘지화학 | Ester-based compound, composition comprising the same, preparation method the composition, and resin composition comprising the composition |
KR101881646B1 (en) * | 2015-08-12 | 2018-07-24 | 주식회사 엘지화학 | Methode of preparing plasticizer composition, and the plasticizer composition prepared thereby |
KR101973123B1 (en) * | 2016-04-22 | 2019-04-29 | 주식회사 엘지화학 | Plasticizer composition and preparation method thereof |
KR102122466B1 (en) * | 2016-07-05 | 2020-06-12 | 주식회사 엘지화학 | Plasticizer, resin composition and method for preparing them |
US10696817B2 (en) | 2016-07-06 | 2020-06-30 | Lg Chem, Ltd. | Plasticizer composition, resin composition and method of preparing the same |
KR102138788B1 (en) * | 2017-09-07 | 2020-07-28 | 주식회사 엘지화학 | Preparing system of ester composition and method of preparing the same using the system |
JP7060414B2 (en) | 2018-03-08 | 2022-04-26 | 花王株式会社 | Plasticizer for halogen-based resins |
US20210363324A1 (en) * | 2018-08-27 | 2021-11-25 | Lg Chem, Ltd. | Plasticizer composition and resin composition including the same |
CN112888732B (en) * | 2018-10-12 | 2022-10-18 | Dic株式会社 | Plasticizer for vinyl chloride resin, vinyl chloride resin composition, electric wire, and vehicle interior material |
ES2944732T3 (en) * | 2019-05-02 | 2023-06-23 | Lg Chemical Ltd | Plasticizing composition and resin composition including the same |
CN114051510B (en) * | 2019-07-03 | 2023-09-12 | 三菱化学株式会社 | Phthalate ester composition |
US20220242814A1 (en) * | 2019-09-27 | 2022-08-04 | Lg Chem, Ltd. | Method for producing diester-based material |
KR102361973B1 (en) * | 2020-04-29 | 2022-02-11 | 애경케미칼주식회사 | Composite plasticizer and polyvinyl chloride resin composition containing the same |
CN116419945B (en) | 2021-01-29 | 2024-06-21 | 株式会社Lg化学 | Plasticizer composition and resin composition containing the same |
WO2023163545A1 (en) * | 2022-02-25 | 2023-08-31 | 주식회사 엘지화학 | Plasticizer composition and resin composition comprising same |
WO2023163546A1 (en) * | 2022-02-25 | 2023-08-31 | 주식회사 엘지화학 | Plasticizer composition and resin composition comprising same |
WO2023163544A1 (en) * | 2022-02-25 | 2023-08-31 | 주식회사 엘지화학 | Plasticizer composition and resin composition comprising same |
Family Cites Families (51)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB851753A (en) * | 1956-11-23 | 1960-10-19 | Union Carbide Corp | Vinyl chloride resin compositions |
US2936320A (en) * | 1957-06-24 | 1960-05-10 | California Research Corp | Diesters of mixed aromatic dibasic acids |
US2975210A (en) | 1958-03-14 | 1961-03-14 | Monsanto Chemicals | Esterification process comprising reacting a mono olefin with an acid ester |
US3096364A (en) * | 1958-12-08 | 1963-07-02 | Monsanto Chemicals | Production of benzyl alkyl phthalates by ester interchange |
US3231642A (en) * | 1964-07-09 | 1966-01-25 | Du Pont | Extrusion and stretching of thermoplastic film |
US3324040A (en) * | 1965-09-17 | 1967-06-06 | Wallace & Tiernan Inc | Homogeneous benzoyl peroxide paste |
BE755297A (en) | 1969-08-27 | 1971-02-26 | Ici Ltd | PLASTICIZING COMPOSITION |
DE2213259B2 (en) * | 1972-03-18 | 1978-03-30 | Dynamit Nobel Ag, 5210 Troisdorf | Process for the production of linear high molecular weight polyesters |
JPS4981449A (en) | 1972-12-11 | 1974-08-06 | ||
DE2701062C3 (en) * | 1976-01-13 | 1987-06-19 | Mitsubishi Gas Chemical Co., Inc., Tokio/Tokyo | Process for the preparation of esters |
US4654390A (en) | 1984-08-10 | 1987-03-31 | The Dow Chemical Company | Monomeric plasticizers for halogen-containing resins |
US4620026A (en) | 1984-08-10 | 1986-10-28 | The Dow Chemical Company | Monomeric plasticizers for halogen-containing resins |
JPS61243845A (en) * | 1985-04-19 | 1986-10-30 | Mitsubishi Gas Chem Co Inc | Polyvinyl chloride resin composition |
JPS63150250A (en) | 1986-12-12 | 1988-06-22 | Toray Ind Inc | Production of dibenzyl phthalates |
JPS6429870A (en) * | 1987-07-24 | 1989-01-31 | Mita Industrial Co Ltd | Controller for bending quantity of form for copying machine |
US4929749A (en) | 1989-03-15 | 1990-05-29 | Synergistics Industries, Limited | Production of terephthalate esters by degradative transesterification of scrap or virgin terephthalate polyesters |
JPH05295206A (en) | 1992-04-23 | 1993-11-09 | Achilles Corp | Agricultural vinyl chloride-based resin film |
JPH05295207A (en) | 1992-04-23 | 1993-11-09 | Achilles Corp | Agricultural vinyl chloride-based resin film |
JPH07157614A (en) | 1993-12-10 | 1995-06-20 | Mitsubishi Chem Corp | Plasticizer composition |
JPH1029870A (en) | 1996-07-16 | 1998-02-03 | Dainippon Ink & Chem Inc | Ceramic green sheet composition |
KR100440738B1 (en) | 1996-07-18 | 2004-10-06 | 주식회사 엘지화학 | Di-2-propylheptyl phthalate useful for plasticizer having excellent physical properties and process for producing the same |
US5686147A (en) | 1996-11-18 | 1997-11-11 | The Goodyear Tire & Rubber Company | Plastisol composition |
JP3728684B2 (en) | 1997-05-30 | 2005-12-21 | 日本ゼオン株式会社 | Vinyl chloride resin composition |
JP2001031794A (en) * | 1999-07-21 | 2001-02-06 | Hokoku Seiyu Kk | Terephthalic ester |
AU2003300377B2 (en) | 2002-10-11 | 2009-04-02 | University Of Connecticut | Blends of amorphous and semicrystalline polymers having shape memory properties |
CN100400499C (en) | 2003-10-31 | 2008-07-09 | 中国石油化工股份有限公司 | Terephthalic acid oxidation residue recovery and utilization method |
CN101107306B (en) * | 2005-01-18 | 2012-06-20 | 埃克森美孚化学专利公司 | Improvements in or relating to plasticiser compositions |
KR100724553B1 (en) | 2005-01-31 | 2007-06-04 | 주식회사 엘지화학 | Plasticizer composition and polyvinyl chloride resin composition containing the same |
US7291748B2 (en) * | 2005-07-28 | 2007-11-06 | Basf Corporation | C10/C7 ester mixtures based on 2-propylheptanol |
US7361779B1 (en) | 2007-04-18 | 2008-04-22 | Eastman Chemical Company | Low-melting mixtures of di-n-butyl and diisobutyl terephthalate |
EP2157159B1 (en) | 2007-04-23 | 2015-12-02 | Idemitsu Kosan Co., Ltd. | Hydraulic fluid |
KR100868194B1 (en) | 2007-05-11 | 2008-11-10 | 주식회사 엘지화학 | Composition of terephthalic acid esters for polymer resin and method for manufacturing the same |
KR100812511B1 (en) | 2007-06-25 | 2008-03-11 | 주식회사 엘지화학 | Vinyl chloride based foam resin composition for nonpoisonous and low-smelling wallcoverings |
KR101123504B1 (en) | 2007-11-08 | 2012-03-09 | 주식회사 엘지화학 | Vinyl chloride based resin composition containing dioctyl terephthalate for covering of electric wire |
CN101878260B (en) * | 2007-11-30 | 2014-07-09 | 埃克森美孚化学专利公司 | C7-C12 secondary alcohol esters of cyclohexanoic acid |
JP5167931B2 (en) | 2008-04-30 | 2013-03-21 | 日立電線株式会社 | Non-halogen flame retardant resin composition and electric wire / cable using the same |
KR101105202B1 (en) | 2009-07-30 | 2012-01-13 | 웅진케미칼 주식회사 | Polymer composition for dye-based polarized film, polarized film using the same and method for preparing the same |
US8791185B2 (en) * | 2010-06-21 | 2014-07-29 | Basf Se | 2-ethylhexyl methyl terephthalate as plasticizer in adhesives and sealants |
JP2012089287A (en) | 2010-10-18 | 2012-05-10 | Yamazol Co Ltd | Vinyl chloride resin composition for coating electric wire/cable |
JP2012092074A (en) | 2010-10-28 | 2012-05-17 | Mitsubishi Gas Chemical Co Inc | Method for producing ester plasticizer |
JP2012255104A (en) | 2011-06-09 | 2012-12-27 | Riken Technos Corp | Vinyl chloride resin composition |
CN102516080A (en) | 2011-09-30 | 2012-06-27 | 白英 | Recovery process of PX oxidation residues and recovery system device thereof |
KR101536380B1 (en) * | 2011-09-30 | 2015-07-14 | 주식회사 엘지화학 | ester plasticizer composition |
EP2644648A1 (en) | 2012-03-30 | 2013-10-02 | LANXESS Deutschland GmbH | Carboxylic acid esters or polyetheresters as a processing aid for fluoro-rubbers |
CN102876275B (en) | 2012-09-20 | 2013-10-02 | 吴江市天源塑胶有限公司 | Adhesive for adhering ceramic and metal |
US9085670B2 (en) * | 2012-10-10 | 2015-07-21 | Lg Chem, Ltd. | Plasticizer, plasticizer composition, heat-resistant resin composition and method for preparing the same |
KR101458311B1 (en) | 2013-04-23 | 2014-11-04 | 주식회사 엘지화학 | Plasticizer, resin composition and method for preparing them |
EP3103788B1 (en) * | 2014-02-07 | 2020-04-01 | LG Chem, Ltd. | Plasticizer composition, method for manufacturing plasticizer composition, and resin composition comprising plasticizer composition |
TWI643844B (en) * | 2014-02-07 | 2018-12-11 | Lg化學股份有限公司 | Plasticizer and resin composition, and preparation method thereof |
ES2955608T3 (en) * | 2015-02-18 | 2023-12-04 | Evonik Oxeno Gmbh & Co Kg | Production of ester mixtures |
KR102019938B1 (en) * | 2015-07-24 | 2019-09-11 | 주식회사 엘지화학 | Plasticizer, resin composition and method for preparing them |
-
2014
- 2014-10-22 TW TW103136575A patent/TWI643844B/en active
- 2014-10-22 KR KR1020140143340A patent/KR101535392B1/en active IP Right Grant
- 2014-10-22 WO PCT/KR2014/009979 patent/WO2015119355A1/en active Application Filing
- 2014-10-22 ES ES14814674T patent/ES2837976T3/en active Active
- 2014-10-22 EP EP14814674.9A patent/EP2927210B1/en active Active
- 2014-10-22 CN CN201911042139.1A patent/CN110734579A/en active Pending
- 2014-10-22 US US14/412,894 patent/US9714211B2/en active Active
- 2014-10-22 CN CN201480001989.6A patent/CN105102418A/en active Pending
- 2014-11-07 KR KR1020140154390A patent/KR20150093580A/en unknown
-
2015
- 2015-02-04 KR KR1020150017581A patent/KR101841813B1/en active IP Right Grant
- 2015-02-04 KR KR1020150017583A patent/KR101705430B1/en active IP Right Grant
- 2015-02-04 KR KR1020150017574A patent/KR101720852B1/en active IP Right Grant
- 2015-02-04 KR KR1020150017584A patent/KR101705431B1/en active IP Right Grant
- 2015-02-04 KR KR1020150017582A patent/KR101705429B1/en active IP Right Grant
- 2015-02-05 JP JP2016547097A patent/JP6402868B2/en active Active
- 2015-02-05 RU RU2016127697A patent/RU2670621C2/en active
- 2015-02-05 TW TW104104010A patent/TWI555732B/en active
- 2015-02-05 EP EP15746898.4A patent/EP3103834B1/en active Active
- 2015-02-05 CN CN201580006654.8A patent/CN105940048B/en active Active
- 2015-02-05 US US15/039,791 patent/US10150727B2/en active Active
Non-Patent Citations (1)
Title |
---|
None * |
Also Published As
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP3103834B1 (en) | Ester composition and method for its manufacturing | |
EP3293226B1 (en) | Plasticizer composition, and resin composition comprising same | |
EP3670593B1 (en) | Plasticizer composition and resin composition | |
EP3272801B1 (en) | Plasticizer composition and resin composition, and method for preparing same | |
EP3434721B1 (en) | Plasticizer composition and resin composition including same | |
KR101952338B1 (en) | Plasticizer composition and resin composition comprising the same | |
EP2851393A1 (en) | Method for preparing ester-based plasticizer, and ester-based plasticizer prepared thereby | |
EP3103788B1 (en) | Plasticizer composition, method for manufacturing plasticizer composition, and resin composition comprising plasticizer composition | |
KR101881646B1 (en) | Methode of preparing plasticizer composition, and the plasticizer composition prepared thereby | |
EP3604417B1 (en) | Citrate-based plasticizer and resin composition including the same | |
EP3342794B1 (en) | Plasticizer composition, resin composition, and preparation method for both compositions | |
EP3296285B1 (en) | Ester-based compound, composition containing same, method for preparing same, and resin composition containing same | |
US11732107B2 (en) | Plasticizer composition including cyclohexane 1,4-diester-based compound and resin composition including the same | |
EP3296286B1 (en) | Ester-based compound, composition containing same, method for preparing same, and resin composition containing same | |
EP3342812B1 (en) | Plasticizer composition, resin composition and method for preparing same |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE |
|
17P | Request for examination filed |
Effective date: 20160701 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
AX | Request for extension of the european patent |
Extension state: BA ME |
|
A4 | Supplementary search report drawn up and despatched |
Effective date: 20161219 |
|
RIC1 | Information provided on ipc code assigned before grant |
Ipc: C08K 5/00 20060101ALI20161213BHEP Ipc: C07C 69/80 20060101ALI20161213BHEP Ipc: C07C 69/82 20060101ALI20161213BHEP Ipc: C08J 3/18 20060101ALI20161213BHEP Ipc: C07C 67/08 20060101ALI20161213BHEP Ipc: C08K 5/12 20060101ALI20161213BHEP Ipc: C07C 69/773 20060101ALI20161213BHEP Ipc: C07C 67/03 20060101ALI20161213BHEP Ipc: C07C 69/76 20060101AFI20161213BHEP |
|
DAX | Request for extension of the european patent (deleted) | ||
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R079 Ref document number: 602015027601 Country of ref document: DE Free format text: PREVIOUS MAIN CLASS: C08K0005109000 Ipc: C07C0067030000 |
|
RIC1 | Information provided on ipc code assigned before grant |
Ipc: C07C 67/08 20060101ALI20181018BHEP Ipc: C07C 67/54 20060101ALI20181018BHEP Ipc: C07C 69/82 20060101ALI20181018BHEP Ipc: C08K 5/00 20060101ALI20181018BHEP Ipc: C07C 69/80 20060101ALI20181018BHEP Ipc: C08K 5/12 20060101ALI20181018BHEP Ipc: C07C 67/03 20060101AFI20181018BHEP |
|
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: GRANT OF PATENT IS INTENDED |
|
INTG | Intention to grant announced |
Effective date: 20181128 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE PATENT HAS BEEN GRANTED |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP Ref country code: AT Ref legal event code: REF Ref document number: 1115544 Country of ref document: AT Kind code of ref document: T Effective date: 20190415 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R096 Ref document number: 602015027601 Country of ref document: DE |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: MP Effective date: 20190403 |
|
REG | Reference to a national code |
Ref country code: LT Ref legal event code: MG4D |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: MK05 Ref document number: 1115544 Country of ref document: AT Kind code of ref document: T Effective date: 20190403 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: HR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 Ref country code: NO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190703 Ref country code: CZ Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 Ref country code: ES Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 Ref country code: LT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 Ref country code: AL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190803 Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BG Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190703 Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190704 Ref country code: LV Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 Ref country code: PL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 Ref country code: RS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: AT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 Ref country code: IS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190803 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 602015027601 Country of ref document: DE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SM Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 Ref country code: IT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 |
|
26N | No opposition filed |
Effective date: 20200106 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: TR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
REG | Reference to a national code |
Ref country code: BE Ref legal event code: MM Effective date: 20200229 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20200205 Ref country code: MC Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20200229 Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20200229 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20200205 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20200229 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190403 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20240122 Year of fee payment: 10 Ref country code: GB Payment date: 20240122 Year of fee payment: 10 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20240123 Year of fee payment: 10 |